RESEARCH
| REPORTS
REFERENCES AND NOTES
SEPARATION MEMBRANES
1. M. B. Smith, J. March, March’s Advanced Organic Chemistry
(Wiley, New York, 2001).
2. Y. Ono, Pure Appl. Chem. 68, 367 (1996).
3. T. Anastas, J. C. Warner, Green Chemistry: Theory and Practice
(Oxford Univ. Press, Oxford, 1998).
4. W. F. von Oettingen, The Halogenated Hydrocarbons of
Industrial and Toxicological Importance (Elsevier, Amsterdam,
New York, 1964).
5. G. Stork, R. Terrell, J. Szmuszkovicz, J. Am. Chem. Soc. 76,
2029–2030 (1954).
6. G. Stork, H. Landesman, J. Am. Chem. Soc. 78, 5128–5129
(1956).
Interfacial microfluidic processing of
metal-organic framework hollow
fiber membranes
Andrew J. Brown,1 Nicholas A. Brunelli,2,3 Kiwon Eum,2 Fereshteh Rashidi,2
7. R. C. Larock, Comprehensive Organic Transformations
(Wiley, New York, 1999).
J. R. Johnson,2 William J. Koros,2 Christopher W. Jones,1,2* Sankar Nair2*
8. F. Dénès, A. Pérez-Luna, F. Chemla, Chem. Rev. 110,
2366–2447 (2010).
9. T. Pei, R. A. Widenhoefer, J. Am. Chem. Soc. 123,
11290–11291 (2001).
10. X. Yao, C.-J. Li, J. Am. Chem. Soc. 126, 6884–6885 (2004).
11. J. J. Kennedy-Smith, S. T. Staben, F. D. Toste, J. Am.
Chem. Soc. 126, 4526–4527 (2004).
12. J. M. Conia, P. Le Perchec, Synthesis 1975, 1–19 (1975).
13. X. Wang, T. Pei, X. Han, R. A. Widenhoefer, Org. Lett. 5,
2699–2701 (2003).
14. Y.-P. Xiao, X.-Y. Liu, C.-M. Che, Angew. Chem. Int. Ed. 50,
4937–4941 (2011).
15. M. Nakamura, T. Hatakeyama, E. Nakamura, J. Am. Chem. Soc.
126, 11820–11825 (2004).
16. L. S. Hegedus, R. E. Williams, M. A. McGuire, T. Hayashi, J. Am.
Chem. Soc. 102, 4973–4979 (1980).
Molecular sieving metal-organic framework (MOF) membranes have great potential for
energy-efficient chemical separations, but a major hurdle is the lack of a scalable and
inexpensive membrane fabrication mechanism. We describe a route for processing MOF
membranes in polymeric hollow fibers, combining a two-solvent interfacial approach for
positional control over membrane formation (at inner and outer surfaces, or in the bulk,
of the fibers), a microfluidic approach to replenishment or recycling of reactants, and an
in situ module for membrane fabrication and permeation. We fabricated continuous
molecular sieving ZIF-8 membranes in single and multiple poly(amide-imide) hollow fibers,
with H2/C3H8 and C3H6/C3H8 separation factors as high as 370 and 12, respectively.
We also demonstrate positional control of the ZIF-8 films and characterize the
contributions of membrane defects and lumen bypass.
17. A. L. Rodriguez, T. Bunlaksananusorn, P. Knochel, Org. Lett. 2,
3285–3287 (2000).
18. S. Majima, Y. Shimizu, M. Kanai, Tetrahedron Lett. 53,
4381–4384 (2012).
19. T. Iwahama, S. Sakaguchi, Y. Ishii, Chem. Commun. (23):
2317–2318 (2000).
20. R. J. Comito, F. G. Finelli, D. W. C. MacMillan, J. Am.
Chem. Soc. 135, 9358–9361 (2013).
21. T. D. Beeson, A. Mastracchio, J. B. Hong, K. Ashton,
D. W. C. Macmillan, Science 316, 582–585 (2007).
22. Y. J. Park, J.-W. Park, C.-H. Jun, Acc. Chem. Res. 41, 222–234
(2008).
23. L. N. Lewis, J. F. Smith, J. Am. Chem. Soc. 108, 2728–2735
(1986).
24. D. A. Colby, R. G. Bergman, J. A. Ellman, Chem. Rev. 110,
624–655 (2010).
25. B. List, Chem. Rev. 107, 5413–5415 (2007).
26. C.-H. Jun, C. W. Moon, Y.-M. Kim, H. Lee, J. H. Lee, Tetrahedron
Lett. 43, 4233–4236 (2002).
olecular sieving membranes have created
interest as high-performance separation
systems for production of petro-based and
renewable fuels and chemicals. Compared
to thermodynamically driven separation
(12), we synthesized ZIF-90 membranes by seeded
growth on the outer surfaces of porous poly-
meric poly(amide-imide) (Torlon) hollow fibers
of ~250-mm outer diameter by immersion in a
methanolic precursor solution at mild condi-
tions (65°C). Free-standing MOF films can also
be synthesized at the interfaces between two im-
miscible solvents (13). However, molecular siev-
ing membranes on the inner surfaces of hollow
fibers also have advantages for rapid, scalable fab-
rication due to the ability to be bundled in close
proximity while avoiding membrane-membrane
contact points and interfaces that lead to defects
during synthesis. Synthesis of selective membranes
in microscopic confined spaces faces a number
of challenges: reactant availability and transport,
positional control of the membrane, and scal-
ability. As the bore size (and hence volume) is
decreased to microscopic dimensions, film for-
mation becomes limited by reactant availability
and local inhomogeneities (14).
We report a methodology for fabricating mo-
lecular sieving MOF membranes (specifically,
ZIF-8), which we refer to as interfacial micro-
fluidic membrane processing (IMMP) (Fig. 1).
IMMP thus combines three key concepts: (i)
in situ ZIF-8 film synthesis in the membrane mod-
ule (Fig. 1A); (ii) a two-solvent interfacial approach
(Fig. 1, B and C) that can be tuned to achieve po-
sitional control over membrane formation (at in-
ner and outer surfaces, as well as inside the bulk,
of the porous fiber); and (iii) the controlled sup-
ply, replenishment, and recycling of reactants at
microfluidic conditions in the hollow fiber bore.
Our approach can be applied more generally to
other MOF materials, but we demonstrate our
key findings here with the example of ZIF-8, which
has been identified as a promising candidate for
important separations such as H2 from hydro-
carbons and propylene from propane (3, 15). To
study the IMMP concept, we designed and fabri-
cated a reusable flow module that serves as
M
methods such as distillation, membrane-based
processes can substantially reduce the energy
and capital costs of separating molecules on a
large scale. Membranes composed of molecular
sieving materials such as zeolites (1), layered ze-
olites (2), or metal-organic frameworks (MOFs)
(3) have intrinsic advantages over polymeric mem-
branes, such as a simultaneously high perme-
ability and selectivity. Despite their performance
limitations, polymeric membranes have contin-
ued to dominate industrial membrane separa-
tions owing to their relative ease of processing
into morphologies such as hollow fibers (4). One
challenge facing molecular sieving membranes is
the lack of an easily scalable, reliable, and benign
fabrication process (5–7). Zeolite membranes are
further hampered by the need for hydrothermal
synthesis on high-cost support materials. MOFs
consist of metal centers connected by coordina-
tion bonds to organic linker molecules. They have
been used to grow crystalline membranes on disk
and tubular substrates through techniques sim-
ilar to those developed for zeolitic membranes
(8). The zeolitic imidazolite framework (ZIF) sub-
class of MOFs is of particular interest for mem-
brane fabrication because of its tunable pore size
and chemistry (9) and relatively good thermal
and chemical stability (10, 11). In an early dem-
onstration of scalable ZIF membrane processing
27. Z. Wang, B. J. Reinus, G. Dong, J. Am. Chem. Soc. 134,
13954–13957 (2012).
28. J. Kwak, Y. Ohk, Y. Jung, S. Chang, J. Am. Chem. Soc. 134,
17778–17788 (2012).
29. D. Sánchez et al., Org. Lett. 14, 536–539 (2012).
30. S. Murai et al., Nature 366, 529–531 (1993).
ACKNOWLEDGMENTS
We thank the University of Texas at Austin and Cancer
Prevention and Research Institute of Texas (R1118) for a start-up
fund and the Welch Foundation (F-1781) and NSF (CAREER:
CHE-1254935) for research grants. A provisional patent based
on this work has been filed by the University of Texas at Austin.
G.D. is a Searle Scholar. We thank V. Lynch for x-ray
crystallography. Metrical parameters for the crystal structures
of compounds S3a to S3g, S3j, S3r, S3s, 4 to 6, and 8 are
available free from the Cambridge Crystallographic Data Centre
under reference numbers CCDC-1003268 to -1003281,
respectively. We thank J. L. Sessler, M. J. Krische, and
D. R. Siegel for loaning chemicals; B. A. Shoulders, S. Sorey, and
A. Spangenberg for NMR advice; Y. Xu for thoughtful suggestions;
A. Dermenci and H. Lim for proofreading the manuscript; and
Z. Dong for checking and repeating the experimental procedure.
SUPPLEMENTARY MATERIALS
1School of Chemistry and Biochemistry, Georgia Institute of
Technology, Atlanta, GA 30332, USA. 2School of Chemical &
Biomolecular Engineering, Georgia Institute of Technology,
Atlanta, GA 30332, USA. 3Department of Chemical and
Biomolecular Engineering, The Ohio State University,
Columbus, OH 43210, USA.
Materials and Methods
Supplementary Text
Table S1
References (31–58)
7 April 2014; accepted 27 May 2014
10.1126/science.1254465
*Corresponding author. E-mail: sankar.nair@chbe.gatech.edu
(S.N.); christopher.jones@chbe.gatech.edu (C.W.J.)
72 4 JULY 2014 • VOL 345 ISSUE 6192
sciencemag.org SCIENCE