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    Applied Catalysis A: General 246 (2003) 193196

    Perspective

    Heterogeneous catalysis: what lies ahead in nanotechnology

    In the past few years, there has been a huge in-

    crease in the interest in nanotechnology, a term that is

    virtually unheard of a decade ago. As nanotechnology

    is increasingly embraced by industrial leaders, theeducated general public, and the government (espe-

    cially the funding agencies), catalysis researchers and

    practitioners begin to employ this term to describe

    their activities. In fact, the length scale of importance

    in heterogeneous catalysis has been known by re-

    searchers to be nanometer or smaller for many years,

    be it the crystallite size of a well-dispersed supported

    noble metal catalyst, the cavity or channel size of a

    zeolite, the ligand size of a coordination complex, or

    the active center of an enzyme. Thus, in many ways,

    nanotechnology has been part of catalysis technology,

    which, when coupled with macroscale reaction engi-

    neering technology, constitute the chemical process

    industry as we know to date.

    However, the phenomenal rise in interest in nan-

    otechnology is not a result of new developments in

    catalysis research. Instead, it results from develop-

    ments in understanding the behavior of ensembles

    of molecules or particles (e.g. self-assembly) and in

    instrumentation and techniques that permit manipu-

    lating and observing matters, molecules, and atoms at

    that scale. Thus, it is fitting to ask how may catalysis

    benefit from this rapid increase in the knowledge ofnanoscience and nanotechnology? Others have of-

    fered their perspectives (e.g.[1]),here we offer ours

    for discussion.

    One area that could receive immediate benefit is

    combinatorial catalysis or high-throughput testing.

    Here, nanotechnology can help miniaturize the equip-

    ment and develop analytical methods to facilitate

    detection of trace quantities of products or occurrence

    of reactions reliably and rapidly. Another potentially

    promising area is catalytic reaction engineering. In

    recent years, various forms of microchannel reactors

    have been fabricated and demonstrated to offer sub-

    stantial advantages in heat transfer characteristic andother attributes [2,3]. Can one reduce a reactor fur-

    ther to nano-size? Imagine a nano-size box-like batch

    reactor with a lid that could be opened and closed

    on demand. Such a reactor, which is of a dimension

    in the order of the mean free path of a molecule,

    may be just large enough to accommodate one set of

    reactant molecules (e.g. one A and one B molecule

    for the reaction A + B C). Then, the only pos-

    sible reaction that can take place in the reactor is

    between them. The selectivity would be 100% at very

    high conversions of the limiting reagent, which is a

    highly desirable goal. Such reactors could be used in

    new application areas such as those that could ben-

    efit from the ability to synthesize and deliver small

    quantities of products to specific locations. An ex-

    ample would be drug delivery into a human body or

    treatment of microbial infection. One could imagine

    adapting the molecular switching technology for the

    openclose motion of the lid. Fabricating such reac-

    tors will be a research challenge, and producing a

    large ensemble of them would be a manufacturing

    challenge.

    Designing and synthesizing a highly selective cat-alyst has been an intriguing and challenging goal in

    catalysis research. The desired properties of a catalyst

    comprise of an active site with the correct ensemble of

    metal atoms, metal ions, or other active components

    such as oxides, carbides, etc., and a cavity around the

    active site that can change configuration to facilitate

    binding of a specific reactant to the active site and ex-

    pulsion of the product. Much effort has been spent in

    attempts to achieve control of these properties. How

    0926-860X/03/$ see front matter 2003 Elsevier Science B.V. All rights reserved.

    doi:10.1016/S0926-860X(03)00023-1

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    194 Perspective / Applied Catalysis A: General 246 (2003) 193196

    may nanoscience and nanotechnology lead us to the

    next level? Here are some possibilities.

    Zeolites are important catalysts due to their acid-

    ity associated with the framework Al ions and shapeselectivity consequent to the molecular-size channels

    and pores. Yet, their synthesis is still based largely

    on empirical knowledge. At present, the specific re-

    lationship between synthesis condition and zeolite

    structure has not been rigorously established and the

    positioning of the Al ions in the framework is not

    well controlled. The formation of the zeolite struc-

    tures is a self-assembly mechanism of aluminate

    and silicate ions around the structure-directing agent.

    Advances in nanoscience may help improve our un-

    derstanding of the arrangement of these ion clusters

    and the structure-directing agent during synthesis

    and how they lead to the final zeolite structure. They

    could improve our ability to design better zeolites

    or other new materials that possess similar desirable

    properties. Rapid advances in material synthesis in

    nanotechnology may offer know-how to incorporate

    Al ions at specific locations.

    Supported metals are another class of widely used

    catalysts. It has been known for many years that

    not all surface atoms of a metal crystallite are alike

    in a catalytic reaction. That is, a reaction may be

    structure-sensitive. The degree of structure sensitivitydiffers, from being rather minor for reactions such as

    hydrogenation on noble metals, to being quite sub-

    stantial for reactions such as ammonia synthesis and

    hydrogenolysis of hydrocarbons [4]. For the latter

    type of reactions, the detailed arrangement of atoms

    on the surface of crystallites of the active compo-

    nent is very important, in addition to the crystallite

    size. Therefore, a desirable goal for catalyst synthesis

    would be to control the surface atomic arrangements

    so as to optimize the desired structure and density

    of the active sites. This would include the ability to,among others, manipulate the deposition of atoms to

    a specific location at a specific rate and order (espe-

    cially for multicomponent catalysts). However, there

    are a number of obstacles to practical applications of

    such an atom-by-atom approach of catalyst synthe-

    sis. If one synthesizes the active sites one at a time,

    and sites of the order of 10161017 are needed for

    bench scale testing, an extremely efficient synthesis

    method will be needed to prepare sufficient samples

    for testing in a reasonable time. Lithography has been

    used to deposit metal clusters in a pattern [5], and

    deposition of small clusters using a STM tip has been

    demonstrated [6]. There is also the possibility for

    scale-up using the millipede technique [7], perhapscoupled with the dip-pen technology. Yet, these tech-

    niques do not offer fine control at the atomic level.

    Thus, new techniques with atomic control that can be

    readily scaled up are needed.

    Even if one succeeded in achieving atomic level

    control during the preparation of metal clusters, there

    is the uncertainty of the stability of the clusters or

    surface structures after exposure to the working envi-

    ronment. If the deposited and desired structure is not

    stable, would rapid structural transformation negate

    the advantages of such an approach? This is a ques-

    tion that awaits an answer. An alternate approach is to

    invent new methods to stabilize the metastable struc-

    ture against restructuring. This is feasible in principle.

    As an example, zeolites are metastable structures.

    Recently, there is increasing recognition of the

    important role that the surrounding environment of

    an active site can play in heterogeneous catalysis.

    Thomas and his coworkers demonstrated that a hex-

    ane molecule can achieve an orientation by nonbond-

    ing interaction with the cavity wall of a Co-AlPO-18

    molecular sieve so as to favor oxidation of the terminal

    carbons and, thus, high selectivity for the adipic acidproduct [8]. Increased selectivity was also reported

    using catalysts prepared with the molecular templat-

    ing technique which enhances favorable interaction of

    the desirable reaction intermediate with the active site

    [9]. The explosion of newly discovered self-assembled

    structures offers unprecedented choice of templates

    for forming cavities of various shapes and sizes. The

    formation of these well-organized, self-assembled

    moieties has been extensively studied. For example,

    a review article by Seidel and Stang [10] outlined

    detailed methodology for forming high-symmetry co-ordination cages using well-defined building blocks

    of specific geometries. Nonetheless, further research

    is needed to adapt such knowledge to catalysis. Then,

    nanotechnology could be used to construct cavities

    that promote certain orientations or conformations of

    reactants and reaction intermediates, thereby facilitat-

    ing activation of particular bonds in the molecule by

    the active site. This situation is similar to that of an

    enzyme in which the protein provides an environment

    for specific interaction with the reactant molecules.

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    Perspective / Applied Catalysis A: General 246 (2003) 193196 195

    Computational studies will be valuable to provide sug-

    gestions of cavity shapes and size for various reactions.

    The concept behind molecular templating has been

    used in conventional zeolite synthesis, namely theuse of structure-directing agents. These agents are

    relatively small molecules and the resulting microp-

    orous zeolites contain regular channels and cavities

    of molecular size. Larger templates such as micelles

    of surfactants or triblock polymers are used for the

    synthesis of mesoporous materials, such as MCM-41

    and SBA-5 [11,12]. More recently, materials con-

    taining regular macropores have been synthesized

    using ordered polystyrene spheres [13]. Formation

    of chiral silica [14] and TiO2 [15] nanotubes have

    been demonstrated using organogel templates. Thus,

    there are techniques to prepare materials contain-

    ing regular channels or cavities of a wide range

    of sizes.

    The meso- and macroporous materials offer much

    lower resistance to molecular diffusion than microp-

    orous solids. Their thin walls are more advantageous

    for rapid solid state transformation than bulk solids.

    Introduction of organic functional groups into the

    channel walls such as in the synthesis of periodic

    mesoporous organosilicas [16] greatly enhances the

    potentials of these materials as useful catalysts. How-

    ever, at present, there is no systematic method to in-troduce or position functional groups that can be used

    to orient a reactant molecule or reaction intermediate,

    as it is the case in an enzyme. New developments are

    needed to overcome this limitation by offering more

    versatile templates and new synthetic techniques.

    New methods to induce self-organization of the tem-

    plates using stronger and controllable forces should

    prove to be very beneficial in providing better control

    of the shape and size of the channels and cavities of

    the final catalyst.

    Another characteristic feature of a protein in anenzyme is its mobility. Proteins often change confor-

    mation upon binding of a reactant and release of a

    product. Such flexibility renders the system the ability

    to accommodate and bind large molecules at multiple

    sites. As of to date, there is practically no inorganic

    system that offers such a flexible framework. A new

    way of thinking will be needed to achieve the effect

    of flexibility. Perhaps concepts, knowledge, and tech-

    niques developed for molecular switching could be

    beneficial here.

    Up until now, we described various possibilities

    that nanoscience and nanotechnology could impact

    on heterogeneous catalysis and catalytic reaction en-

    gineering. We have identified a number of technicaldevelopments or inventions needed to bring them to

    fruition. In order to make these possibilities a prac-

    tical reality, the cost of production must also be con-

    sidered. Although any cost estimate in the absence of

    the technology is highly speculative, one possibility is

    that nanotechnology in catalysis would follow a sim-

    ilar path as microelectronics. Thus, the initial impact

    would be on specialty applications of low volume and

    high cost. With proven benefits, increasing demands,

    and improved techniques, the cost of manufacturing

    would drop rapidly with maturity of the technology.

    Then, the practice of catalysis and catalytic reaction

    engineering would reach a new state unimaginable a

    few decades ago.

    Acknowledgements

    This work was supported by the Department of En-

    ergy, Office of Science, Basic Energy Sciences. Very

    insightful comments by Professors Robert Davis and

    Raymond Gorte are also acknowledged.

    References

    [1] G.A. Somorjai, Y.G. Borodko, Catal. Lett. 76 (2001) 1.

    [2] R.S. Wegeng, A.L.Y. Tonkovcich, Y. Wang, S. Fitzgerald,

    M.J. LaMont, D.P. VanderWiel, J.L. Zilka, Microchannel

    Reactors for Automotive Fuel Processors, http://www.pnl.gov/

    microcats/aboutus/research/ott.gov, 2001.

    [3] M.W. Losey, M.A. Schmidt, K.F. Jensen, Microfabricated

    multiphase packed-bed reactors: characterization of mass

    transfer and reactions, I&EC Res. 40 (2001) 25552562.

    [4] R.I. Masel, Principles of Adsorption and Reaction on Solid

    Surfaces, Wiley, New York, NY, 1996, Chapter 6;G.A. Somorjai, Introduction to Surface Chemistry and

    Catalysis, Wiley, New York, NY, 1994, Chapter 7.

    [5] T. Tsirlin, J. Zhu, J. Grunes, G.A. Somorjai, Top. Catal. 19

    (2002) 165.

    [6] D.M. Kolb, Surf. Sci. 500 (2002) 722.

    [7] P. Vettinger, G. Cross, M. Despont, U. Drechsler, U. Drig,

    B. Gotsmann, W. Hberle, M.A. Lantz, H.E. Rothuizen, R.

    Stutz, G.K. Binnig, IEEE Trans. Nanotechnol. 1 (2002) 39.

    [8] J.M. Thomas, R. Raja, G. Sankar, R.G. Bell, Nature 398

    (2000) 227;

    R. Raja, J.M. Thomas, J. Mol. Catal. A 181 (2002) 3.

    [9] K. Polborn, K. Severin, Chem. Commun. (1999) 2481.

    http://www.pnl.gov/microcats/aboutus/research/ott.govhttp://www.pnl.gov/microcats/aboutus/research/ott.govhttp://www.pnl.gov/microcats/aboutus/research/ott.govhttp://www.pnl.gov/microcats/aboutus/research/ott.govhttp://www.pnl.gov/microcats/aboutus/research/ott.gov
  • 8/12/2019 01 - 2003 - Kung, Ap Cat A Gen, V246, P193.pdf

    4/4

    196 Perspective / Applied Catalysis A: General 246 (2003) 193196

    [10] S.R. Seidel, P.J. Stang, Acc. Chem. Res. 35 (2002) 972.

    [11] J.S. Beck, J.C. Vartuli, W.J. Roth, M.E. Leonowicz, C.T.

    Kresge, K.D. Schmitt, C.T.-W. Chu, D.H. Olson, E.W.

    Sheppard, S.B. McCullen, J.B. Higgins, J.L. Schlenker, J.

    Am. Chem. Soc. 114 (1992) 10834.[12] P. Yang, D. Zhao, D.I. Margolese, B.F. Chmelka, G.D. Stucky,

    Chem. Mater. 11 (1999) 2813.

    [13] R.C. Schroden, C.F. Blanford, B.J. Melde, B.J.S. Johnson, A.

    Stein, Chem. Mater. 13 (2001) 1074.

    [14] J.H. Jung, Y. Ono, S. Shinkai, Chem. Eur. J. 6 (2000) 4552.

    [15] J.H. Jung, H. Kobayashi, K.J.C. van Bommel, S. Shinkai, T.

    Shimizu, Chem. Mater. 14 (2002) 1445.

    [16] M.J. MacLachlan, T. Asefa, G.A. Ozin, Chem. Eur. J. 6

    (2000) 2507.

    Harold H. Kung, Mayfair C. Kung

    Department of Chemical Engineering

    Northwestern University, 2145 Sheridan Road

    Evanston, IL 60208-3120, USACorresponding author.E-mail address: [email protected]

    (H.H. Kung)

    1 December 2002