Download presentation
Presentation is loading. Please wait.
Published byEvan Bridges Modified over 9 years ago
1
Anna C. Balazs Jae Youn Lee Gavin A. Buxton Olga Kuksenok Kevin Good Valeriy V. Ginzburg* Chemical Engineering Department University of Pittsburgh Pittsburgh, PA *Dow Chemical Company Midlland, MI Multi-scale Modeling of Polymeric Mixtures
2
Use Multi-scale Modeling to Examine: Reactive A/B/C ternary mixture A and B form C at the A/B interface Critical step in many polymerization processes Challenges in modeling system: Incorporate reaction Include hydrodynamics Capture structural evolutional and domain growth Predict macroscopic properties of mixture Results yield guidelines for controlling morphology and properties
3
A and B are immiscible Fluids undergo phase separation C forms at A/B interface Alters phase-separation Examples: Interfacial polymerization Reactive compatibilization Two order parameters model: here is density Challenges: Modeling hydrodynamic interactions Predicting morphology & formation of C System C B A
4
Free Energy for Ternary Mixture: F L Free energy F = F L + F NL Coefficients for F L yield 3 minima Three phase coexistence A B C
5
Free Energy : Non-local part, F NL Free energy F= F L + F NL Reduction of A/B interfacial tension by C: No formation of C in absence of chemical reactions ( ) Cost of forming C interface:. For (no reactions & no C) Standard phase-separating binary fluid in two-phase coexistence region
6
Evolution Equations * Order parameters evolution: Cahn –Hilliard equations M w (A) = M w (B); M w (C) = 2* M w (A) Navier-Stokes equation * C. Tong, H. Zhang, Y.Yang, J.Phys.Chem B, 2002
7
Lattice-Boltzmann Method D2Q9 scheme 3 distribution functions Macroscopic variables: Constrains & Conservation Laws Governing equations in continuum limit are: Cahn –Hilliard equations Navier-Stokes equation
8
Single Interface: System behavior vs, Higher leads to wider C layer Choose parameters to have narrow interface Need other parameters and additional non-local terms to model wide interfaces. Steady-state distributions:
9
Diffusive Limit: No Effects of Hydro Initial state: 256 x 256 sites High visc. No reaction Domain growth Turn on reaction when R =4 W/reactions: steady-states Reactions arrest domain growth
10
Viscous Limit: Effect of Hydrodynamics No reaction Domain growth Evolution w/reactions:, Domain growth slows down but does not stop Velocities due to Advect interfaces and prevent equilibrium between reaction & diffusion
11
Compare Morphologies Diffusive regime: Steady-state Viscous regime: Early time Viscous regime: Late times
12
Domain Growth vs. Reaction Rate Ratio, R(t) vs. time for different Diffusive limit: Freezing of R due to interfacial reactions Viscous limit: Growth of R slows down, especially at early times R smaller for greater
13
Viscous Limit: Evolution of Average Interface Coverage, I C. I c = (L 2 / L AB ) = R I C saturates quickly; value similar in diffusive and viscous limits Domain growth freezes in diffusive limit I C = const for different R in viscous regimes 21
14
Viscous Limit: Evolution of Avg. Amount of C: At early times, is the similar in both cases until I C saturates At late times, is smaller in viscous regime than in diffusive Velocity advects interfaces larger for greater
15
Dependence on Reaction Rates: Diffusive Regime, Reaction rates: a) ( ) b) ( ) c) ( ) Steady-state : The higher the reaction rates, the faster the interface saturates The lower the saturated value of R (b) (c)
16
Dependence on Reaction Rates: Viscous Regime, No saturation of R R(t) smaller for higher reaction rates
17
Dependence on Reaction Rates, & Interface Coverage, I C Value of depends on values of reaction rates Higher reaction rates yield greater Sat. of I C faster for higher reaction rates Values similar for different cases
18
Morphology Mechanical Properties Output from morphology study is input to Lattice Spring Model (LSM) LSM: 3D network of springs Consider springs between nearest and next-nearest neighbors Model obeys elasticity theory Different domains incorporated via local variations in spring constants Apply deformation at boundaries Calculate local elastic fields
19
Determine Mechanical Properties Use output from LB as input to LSM Morphology Strain Stress
20
Symmetric Ternary Fluid; Local in 3 phase coexistence; Cost of A/C and B/C interfaces ( ) Viscous limit,
21
Conclusions Developed model for reactive ternary mixture with hydrodynamics Lattice Boltzmann model Compared viscous and diffusive regimes Freezing of domain growth in diffusive limit and slowing down in viscous limit R(t) depends on and specific values of reaction rates Future work: “Symmetric” ternary fluids A & B & C domain formation Determine mechanical properties
Similar presentations
© 2025 SlidePlayer.com. Inc.
All rights reserved.