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High Aspect Ratio Polymer Nanopore Membranes by Conformal Initiated Chemical Vapor Deposition

Written by: 
Jeff Morse, PhD
Recently, Asatekin and Gleason from MIT reported on their work using conformal initiated chemical vapor deposition (iCVD) to control the size and surface functionality of polymeric nanopores. Their work demonstrates a simple, scalable nanomanufacturing process to synthesize nanopore membranes for separation of small molecules. Utilizing a facile approach to tune the pore size, shape, and surface chemical properties, an approach to customize membrane properties for a range of separations applications has been developed. Additional models have been developed by the authors to better understand the conformal deposition processes for ultra-high aspect ratio nanopores. These models will be instrumental for further investigations of the range of monomers and initiators that can be used for the iCVD process.

Reviewed by Jeff Morse, PhD, National Nanomanufacturing Network

  • Asatekin A, Gleason KK. 2011. Polymeric Nanopore Membranes for Hydrophobicity-Based Separations by Conformal Initiated Chemical Vapor Deposition. Nano Letters 11:677-686. doi:10.1021/nl103799d

The use of porous membranes provides a scalable, low cost energy efficient approach to industrial scale separations, such as size-based sieving or desalination by reverse osmosis.Membrane separation using these techniques is particularly challenging for the case of small molecules of similar size ranges. For biological and pharmaceutical applications, these approaches to separations become important as industrial scale techniques are required to replace present methods such as chromatography. Additionally, molecular fractionation can also occur during sieving operation. Membranes that can enable separations based on other chemical properties, for instance hydrophobicity, could extend the range of applications using these techniques. In order to achieve such membrane performance, the pore diameters need to be similar in size to the molecules being separated, with controlled surface composition and functionality. In this manner the permeation of the molecules through the pore is dominated by interactions of the molecule with the pore wall, thus solutes that adsorb more strongly to the pore surface are partitioned more into the pore and permeate more rapidly. Thus separation based on both size and chemical structure can be achieved. Previous approaches to achieve such pore structures have utilized atomic layer deposition (ALD) of silicon dioxide to narrow the pores of anodized aluminum oxide (AAO) membranes, then functionalized the pore surface using silane. Similarly, nanotubes were formed by electroless deposition of gold within an AAO template and subsequently functionalized with a self-assembled monolayer (SAM). While these techniques offer a means to controllably tune the diameter of the nanopore down to the few nanometers range, and subsequently control the chemical properties of the pore surface, the synthesis processes require high temperatures. Additionally, the processes may not be environmentally friendly, and are costly to scale. A scalable, low cost method of forming nanopore membranes with controlled surface chemistry is necessary to address present and future industrial needs.

Schematic describing the two types of membranes prepared in this study. Single layer membranes (top) are formed in one step by iCVD from PFDA (green), a fluorinated monomer, onto track-etched membranes. Depending on the deposition conditions used, the pPFDA layer may decrease in thickness proceeding into the pore (top, right), resulting in a nanopore with a bottleneck cross section. The first layer in two-layer membranes (bottom) is a cross-linked film of pDVB (red) and is used for narrowing the pores to the desired diameter. The second layer is once again pPFDA. Although for clarity in the schematic both layers are shown with similar thickness, the actually bilayer membranes utilized a much thinner pPFDA layer. The resulting narrow cylindrical pore (bottom, right) would be achieved when both depositions are conformal.
Recently, Asatekin and Gleason from MIT reported on their work using conformal initiated chemical vapor deposition (iCVD) to control the size and surface functionality of polymeric nanopores. iCVD effectively translates free radical polymerization into a CVD process. The substrate being coated is mounted on a cooled stage in a low vacuum reactor. A thermally labile initiator and one or more monomers are fed into the reactor in the vapor phase. Free radicals are generated from the initiator by heated filaments positioned above the cooled substrate. The free radical and monomer molecules adsorb onto the cooled substrate and polymerization is initiated. Since the reactants are delivered in the vapor phase, uniform conformal coatings are possible on virtually any substrate without the need for solvents or hazardous chemicals. Furthermore, the process is scalable to large areas, and adaptable to platforms such as roll-to-roll processing. In this investigation, the authors focused on membrane separations based on hydrophobicity, utilizing the fluorinated monomer perfluorodecyl acrylate (PFDA) to functionalize the pore surface. An initial single step iCVD process was used to narrow down the 50 nm pores of a tracked polycarbonate membrane. Two samples were prepared having 5 nm and 9 nm pore diameters. A two-step deposition process was also investigated where the pore narrowing monomer was first deposited, followed by the surface functionalizing monomer. By decoupling the pore narrowing step from surface functionalization, it is possible to obtain a more uniform coating along the length by using a monomer having a better balance between surface diffusion along the pore surface and initiation of polymer cross-linking. In this approach, the authors first deposited poly-(divinylbenzene) (pDVB) to narrow the pore diameter, followed by pPFDA to functionalize the pore surface. The resulting narrowed pore structured showed a conformal, uniform pore structure using the two layer approach, with pore diameter ~5 nm and aspect ratio of ~4000. In comparison, the single layer coating approach achieved uniform pores having diameters as small as 5 nm, but the pore structure was bottlenecked resulting in larger pore diameters deeper within the pore. In order to tune the physical and chemical properties of the nanopores, several parameters can be varied, including substrate temperature, reaction pressure, partial pressure of reactants, and selection of monomers and initiator.

In order to characterize the permeation properties and separation selectivity of the hydrophobic nanopore membrane structures, two sets of similar sized small molecules were selected with different levels of hydrophobicity. Comparison of the results for the different nanopore structures illustrated that the two layer conformally coated nanopores exhibited the highest diffusion selectivity, ranging from 2-4 times greater than that of the single layer nanopores having the same diameter. Furthermore, to illustrate the impact of hydrophobicity on diffusion selectivity, the two layer conformal nanopore structures exhibited 10-25 times greater selectivity than the nanopore membrane with only the pDVB coating. Thus a simple, scalable nanomanufacturing process has been demonstrated to synthesize nanopore membranes for separation of small molecules. Utilizing a facile approach to tune the pore size, shape, and surface chemical properties, an approach to customize membrane properties for a range of separations applications has been developed. Additional models have been developed by the authors to better understand the conformal deposition processes for ultra-high aspect ratio nanopores. These models will be instrumental for further investigations of the range of monomers and initiators that can be used for the iCVD process.

Figure reprinted with permission from Asatekin A, Gleason KK. 2011. Polymeric Nanopore Membranes for Hydrophobicity-Based Separations by Conformal Initiated Chemical Vapor Deposition. Nano Letters 11:677-686. doi:10.1021/nl103799d Copyright 2011 American Chemical Society.