Current Research Interests - Professor E. Bruce Nauman
Nanoparticles, Nanobiotechnology,
Nanothermodynamics and Nanofluidics
This collection of neologisms is more
than buzzwords. There are very real and
different phenomena that become important on size scales of 10 to 100 nanometers. The ordinary chemical potential must be
augmented with a gradient term, phase boundaries depend on the size of the system, and the
time-average interface between phases is a smooth function.
Multiphase systems have minimum structure sizes, and the fluid mechanics of
multiphase systems can be treated using a single equation of motion that contains a
concentration dependent body force. Although
some of these facts date to van der Waals, they
are just now becoming generally recognized. They
offer great potential for guiding the creation of novel structures and new commercial
products. Our work has centered on nano dispersions of
one polymer in another and most recently on the dispersion of proteins in polymer matrices
for drug delivery, biocatalysis, and bioactive scaffolds for tissue engineering. Other applications-orientated projects include polymer nanocomposites and the manufacture
of nanoparticles from organic compounds having molecular weights as low as a few hundred. Theoretical work includes studies on surface
enrichment, concentration enhancement in nanopores, and fluid mechanics in small, confined
spaces.
Pretty Picture 1
Pretty Picture 2
Multicomponent Diffusion, MD and DPD
Simulations
Both
practical and conceptual problems arise in standard theories of multicomponent diffusion. These include the sometimes arbitrary and even
artificial selection of one component as the solvent, the lack of explicit dependence on
the properties of the solvent, and the difficulty in formulating compositionally dependent
diffusion coefficients that satisfy material balance constraints. Two alternative approaches based on self-diffusion
coefficients for the various components are physically reasonable and overcome these
difficulties. The approaches differ in the
extent of cross diffusion that is predicted. Either
approach can be used in systems where the component diffusivities differ greatly in
magnitude and where the number of chemical species is large, as in polymerizations. We have begun testing these theories for ternary
systems using molecular dynamics (MD) and dissipative particle dynamics (DPD) simulations. The MD simulations are theoretically sound but
computationally demanding. Attention is
restricted to relatively low molecular weight hydrocarbons such as C8 to C16
alkanes. DPD is more speculative but
offers hope of going to longer chain lengths by proper adjustment of the simulation
constants.
The Systematic Design of Polymer
Blends
The economic potential of
well-formulated polymer blends is known, but the research avenues for achieving this
potential remain largely Edisonian. A better,
systematic approach is becoming possible. The
first step in this new approach is the accurate prediction of blend morphologies, for
example, cocontinuous, particulate, two phases particulate, and core-shell structures.
This step has been largely accomplished. The
morphologies are usually self-similar, and control of the absolute size of the predicted
structures becomes the next issue. Phase
growth or ripening can be controlled through chemical pinning or by the use of random or
block copolymers as interfacial agents. The
latter also provides the interfacial adhesion needed in most systems for best performance. "Almost a priori" theories for
predicting optimal types and concentrations of interfacial agents have recently been
developed. The use of random copolymers is
particularly interesting since they are often much cheaper than diblocks. The final step in designing polymer blends is
relating the stabilized morphology to properties valuable in commercial applications. This is becoming possible in structural
applications where performance depends on impact strength and modulus. Super-high impact polymers with properties greatly
exceeding those in commercial materials have been created.
Opportunities remain to be exploited in more specialized applications and
markets.
The Dynamics of Phase Ripening
>In
many binary blends of immiscible polymer, a pronounced increase in the size of the
dispersed droplets has been found during their annealing in the molten state. Two ripening
mechanisms are recognized in a quiescent particulate system: Ostwald ripening and Brownian
coalescence. Ostwald ripening, also know as the evaporation condensation mechanism, is described using the modified Cahn-Hilliard
equation. The particle size distribution is found to be self-similar and broadened with
increasing volume fraction of the minor phase.
The coalescence of
droplets has been studied extensively but the final step in the coalescence process has
been a mystery. Hydrodynamics predict that
the droplets slow in their approach but never quite touch, much like a Greek paradox. A semi-empirical argument based on van der Waal's
forces resolves the paradox for some but provides no physical insight. Nonlinear diffusion provides the answer and
suggests methods for controlling coalescence rates. The
interstitial fluid has a higher chemical potential and literally diffuses out of the way. We can enhance or retard coalescence by adding
components which concentrate at interfaces and alter chemical potentials. There are many and potentially cheaper
possibilities than using conventional amphiphiles such as detergents and block copolymers. Our work applies directly to polymer systems but
are conceptually applicable to small molecules as well.
Other Topics
Current efforts include polymer
reaction engineering of anionic, free radical and condensation polymerizations; theory and
simulation of spinodal decomposition; use of Visual Basic for user friendly process
models; recycling of mixed plastics, and flash devolatilization of polymers. A new
form of motionless mixer (a.k.a. static mixer) is being built and tested as part of a
colorborative effort with IIT Delhi. It is designed to promote axial mixing.
Most static mixers are designed to promote radial mixing.