Abstract
The influence of flow on the free energy of polymer solutions is examined from several points of view both on macroscopic and microscopic bases. Application of non-equilibrium chemical potential to the phenomena of flow-induced phase separation and thermodynamically induced polymer degradation is reviewed. Polymer degradation under elongational flow was extensively covered in a recent review in this series. The thermodynamic theory is compared with the dynamical approaches used in the analysis of stability of solutions and it is seen under which conditions the criteria defining the spinodal line under shear (i.e. the limit of the stability region) are the same in both approaches. The thermodynamic analysis may be useful due to its greater simplicity though, in contrast, the details of the phase segregation or homogenisation and the analysis of the dynamical aspects (viscosity, light scattering) are beyond the reach of a strictly thermodynamic method. A short summary of the phenomenology of flow-induced changes in the phase diagram of polymer solutions under flow is given. Perspectives and open problems are pointed out.
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Abbreviations
- A:
-
affinity
- A:
-
matrix of kinetic constants
- ai :
-
activity of the species i
- aα :
-
the droplet radius
- b:
-
length of a segment of the polymer
- B:
-
matrix including the hydrodynamic effects or matrix of kinetic constants
- c:
-
number of moles per unit volume
- \(\tilde c\) :
-
reduced concentration defined as [η]c
- d:
-
slope of the curve η(\(\dot \gamma\)) with a change of sign
- D:
-
curvilinear diffusion coefficient
- DT :
-
effective diffusion coefficient in the shear direction
- D 2 :
-
polymer self-diffusion coefficient
- E:
-
deformation gradient tensor
- f:
-
specific Helmholtz free energy
- F:
-
force or thermodynamic force
- g:
-
Gibbs free energy per unit volume
- G*(ω):
-
complex stress-strain coefficient
- ΔG M :
-
Flory-Huggins mixing Gibbs free energy
- ΔG s :
-
non-equilibrium contribution to the Gibbs free energy
- H:
-
elastic constant
- J*(ω):
-
complex compliance
- J:
-
steady-state compliance
- J1, J:
-
diffusion fluxes
- J s :
-
entropy flux
- k′:
-
entropic elastic constant
- kij :
-
kinetic constant for the breaking of a macromolecule P j to give P i
- Kij :
-
chemical equilibrium constant defined by the rate k ij /κij
- l:
-
length of the duct
- m:
-
ratio of the partial molar volume of the polymer to one of the solvent
- M:
-
molecular weight
- Mn :
-
number average for the molecular weight of the polymer
- Mw :
-
weight average for the molecular weight of the polymer
- M o :
-
molecular weight of a monomer
- n:
-
number of molecules per unit volume (or number density)
- ni :
-
number of moles of the species i
- N:
-
number of segments in a polymer
- NA :
-
Avogadro's number
- ñ 1 :
-
number of moles of the solvent
- ñ 2 :
-
number of moles of the solute
- \(N_i^{(\dot \gamma )}\) :
-
number of chains with i monomers under a shear
- p:
-
pressure
- Δp :
-
pressure difference
- P v :
-
viscous pressure tensor
- P v ij :
-
components of the viscous pressure tensor
- Pi :
-
chain with i monomers
- q:
-
parameter for defining what kind of averaged molecular weight is used
- Q:
-
flow rate
- Qi :
-
normal modes of the chain
- r:
-
distance to the axis of a duct
- R:
-
constant of gases
- R:
-
the end-to-end vector or the radius of the duct
- R i :
-
the vector from bead i to bead i + 1
- s:
-
specific entropy
- T:
-
absolute temperature
- Tc :
-
critical temperature
- Tr:
-
trace of a tensor
- u:
-
specific internal energy
- u:
-
the local deformation vector
- v:
-
specific volume
- v:
-
velocity vector
- V:
-
symmetric part of velocity gradient
- xi :
-
molar fraction of the species i
- W:
-
configuration tensor
- z:
-
coordination number
- α:
-
parameter of the most probable distribution or the friction coefficient
- \(\dot \varepsilon\) :
-
the extensional rate
- εij :
-
component of the strain tensor
- ζ:
-
friction coefficient
- Γ:
-
gamma function
- \(\dot \gamma\) :
-
the shear rate
- γ 0 :
-
amplitude of the oscillatory shear strain
- \(\dot \gamma ^0\) :
-
amplitude of the oscillatory shear rate
- γ′:
-
infinitesimal displacement gradient in the polymer phase
- \(\dot \gamma _c\) :
-
critical shear rate
- \(\dot \gamma _w\) :
-
shear rate at the wall
- γ (0)αβ :
-
interfacial tension in the absence of flow
- \(\dot \gamma _{0.8}\) :
-
shear rate for which η (\(\dot \gamma\)) is equal to 80% of η0
- η:
-
shear viscosity
- ηs :
-
viscosity of the pure solvent
- η 0 :
-
viscosity for zero shear rate
- η*(ω):
-
complex viscosity
- [η]:
-
intrinsic viscosity
- Θ:
-
theta temperature
- ϑ:
-
the effective flexibility parameter
- κ ij :
-
kinetic constant for the recombination of chains
- λ:
-
correction to the chemical equilibrium reaction by effect of shear
- λi :
-
eigenvalues of the matrix B
- μi :
-
chemical potential of species i
- μ 0i :
-
reference chemical potential of species i
- μ (s)i :
-
non-equilibrium contribution to the chemical potential of i
- μ 1s :
-
non-equilibrium contribution to the solvent chemical potential
- μ p2 :
-
chemical potential under constant P v12
- \(\mu _{\dot \gamma 2}\) :
-
chemical potential under constant \(\dot \gamma\)
- μ w2 :
-
chemical potential under constant W
- vi :
-
stoichiometric coefficient of i
- π:
-
osmotic pressure
- πφ :
-
equilibrium contribution to the osmotic pressure
- πel :
-
non-equilibrium contribution to the osmotic pressure
- σ:
-
the stress tensor
- τ:
-
relaxation time
- τd :
-
disengagement time
- φ:
-
volume fraction of polymer
- χ:
-
Flory's interaction parameter
- ψ:
-
the configurational distribution function
- ψ 0 :
-
the equilibrium distribution function
- \(\Psi _1 (\dot \gamma )\) :
-
the first normal stress coefficient
- \(\Psi _2 (\dot \gamma )\) :
-
the second normal stress coefficient
- ω:
-
angular frequency
- Ω:
-
solid angle
- Ω:
-
orthogonal matrix to diagonalize B
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Jou, D., Casas-Vázquez, J., Criado-Sancho, M. (1995). Thermodynamics of polymer solutions under flow: Phase separation and polymer degradation. In: Physical Properties of Polymers. Advances in Polymer Science, vol 120. Springer, Berlin, Heidelberg. https://doi.org/10.1007/3-540-58704-7_4
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