TY - JOUR
T1 - Fluid convection driven by surface tension during free-surface frontal polymerization
AU - Gao, Yuan
AU - Paul, Justine E.
AU - Chen, Manxin
AU - Seth, Aarav
AU - Liu, Qibang
AU - Hong, Liu
AU - Chamorro, Leonardo P.
AU - Ewoldt, Randy H.
AU - Sottos, Nancy R.
AU - Geubelle, Philippe H.
N1 - This work was supported by the U.S. Air Force Office of Scientific Research through Award FA9550-20-1-0194 as part of the Center of Excellence in Self-healing and Morphogenic Manufacturing. The authors also acknowledge the support of the National Science Foundation for Grant No. 1933932 through the GOALI: Manufacturing USA: Energy Efficient Processing of Thermosetting Polymers and Composites.
PY - 2024/7
Y1 - 2024/7
N2 - Frontal polymerization (FP) is an efficient method to manufacture thermoset polymers and composites, and is usually modeled as a reaction–diffusion (RD) process. In this study, we investigate numerically and experimentally how fluid convection ahead of the propagating front can impact the reaction–diffusion balance in the free-surface FP of dicyclopentadiene (DCPD) and 5-ethylidene-2-norbornene (ENB). Multiphysics finite element analyses reveal how the velocity of the surface-tension-driven flow described by the dimensionless Marangoni number can be modulated by varying the processing temperature and the viscosity of the monomer resin. The surface-tension-driven fluid velocity exhibits two distinct regimes, which arise from the interplay and competition between thermal and chemical advection. The dispersion of the reaction heat by the Marangoni flow leads to a reduction in the velocity of the front. The presence of fluid convection during FP can lead to instabilities in the front propagation and generate reaction patterns, which can be adjusted by controlling the initial temperature and degree of cure. The numerical findings are corroborated by experiments that combine FP and particle image velocimetry (PIV).
AB - Frontal polymerization (FP) is an efficient method to manufacture thermoset polymers and composites, and is usually modeled as a reaction–diffusion (RD) process. In this study, we investigate numerically and experimentally how fluid convection ahead of the propagating front can impact the reaction–diffusion balance in the free-surface FP of dicyclopentadiene (DCPD) and 5-ethylidene-2-norbornene (ENB). Multiphysics finite element analyses reveal how the velocity of the surface-tension-driven flow described by the dimensionless Marangoni number can be modulated by varying the processing temperature and the viscosity of the monomer resin. The surface-tension-driven fluid velocity exhibits two distinct regimes, which arise from the interplay and competition between thermal and chemical advection. The dispersion of the reaction heat by the Marangoni flow leads to a reduction in the velocity of the front. The presence of fluid convection during FP can lead to instabilities in the front propagation and generate reaction patterns, which can be adjusted by controlling the initial temperature and degree of cure. The numerical findings are corroborated by experiments that combine FP and particle image velocimetry (PIV).
KW - Frontal polymerization
KW - Particle image velocimetry
KW - Reaction–diffusion-convection system
KW - Surface-tension-driven flow
KW - Thermo-chemical instability
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U2 - 10.1016/j.mechmat.2024.104987
DO - 10.1016/j.mechmat.2024.104987
M3 - Article
AN - SCOPUS:85190749755
SN - 0167-6636
VL - 194
JO - Mechanics of Materials
JF - Mechanics of Materials
M1 - 104987
ER -