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Rheological properties of reactive polymer melts.
Authors:Z Kembłowski  J Torzecki
Institution:(1) Institute of Chemical Engineering, Lódzacute Technical University, ul. Wólczanacuteska 175, PL-90-924 Lstrokódzacute, Poland
Abstract:A new method for describing the rheological properties of reactive polymer melts, which was presented in an earlier paper, is developed in more detail. In particular, a detailed derivation of the equation of a first-order rheometrical flow surface is given and a procedure for determining parameters and functions occurring in this equation is proposed. The experimental verification of the presented approach was carried out using our data for polyamide-6.Notation E Dimensionless reduced viscosity, eq. (34) - E 0 ldquoNewtonianrdquo asymptote of the function (36) - E infin ldquopower-lawrdquo asymptote of the function (36) - E Gcy = 1 the value ofE atGcy = 1 - k degradation reaction rate constant, s–1 - k 1 rate constant of functionphiv (t), eq. (26), s–1 - k 2 rate constant of functionpsgr (t), eq. (29), s–1 - K(t) residence-time-dependent consistency factor, eq. (22) - M w weight-average molecular weight - M x x-th moment of the molecular weight distribution - R gas constant - S x M x /M w - t residence time in molten state, s - t j thej-th value oft, s - T temperature, K - % MathType!MTEF!2!1!+-% feaafiart1ev1aaatCvAUfeBSjuyZL2yd9gzLbvyNv2CaerbuLwBLn% hiov2DGi1BTfMBaeXatLxBI9gBaerbd9wDYLwzYbItLDharqqtubsr% 4rNCHbGeaGqiVu0Je9sqqrpepC0xbbL8F4rqqrFfpeea0xd9vqpe0x% c9q8qqaqFn0dXdir-xcvk9pIe9q8qqaq-xir-f0-yqaqVeLsFr0-vr% 0-vr0db8meaabaqaciGacaGaaeqabaWaaeaaeaaakeaaieGaceWFZo% Gbaiaaaaa!3B4E!\\dot \gamma \] shear rate, s–1 - 
$$\dot \gamma _i$$
i thei-th value of 
$$\dot \gamma$$
, s–1 - 
$$\dot \gamma _{r = 1}$$
r =1 the value of 
$$\dot \gamma$$
atGcy = 1, s–1 - 
$$\dot \gamma ^*$$
* reduced shear rate, eq. (44), s–1 - Gcy dimensionless reduced shear rate, eq. (35) - eegr viscosity, Pa · s - 
$$\eta (\dot \gamma ,t)$$
shear-rate and residence-time dependent viscosity, Pa · s - 
$$\eta _{\dot \gamma \to 0} (t)$$
zero-shear-rate degradation curve - 
$$\eta _{\dot \gamma _1 } (t)$$
degradation curve at 
$$\dot \gamma _i$$
- eegr trarr0 (t) zero-residence-time flow curve - 
$$\eta _{t \to 0} (\dot \gamma ,t)$$
ldquoNewtonianrdquo asymptote of the RFS - 
$$\eta _{t_j } (\dot \gamma )$$
instantaneous flow curve - 
$$\eta _{\dot \gamma \to \infty } (\dot \gamma ,t)$$
ldquopower-lawrdquo asymptote of the RFS - eegr 0,0 zero-shear-rate and zero-residence-time viscosity, Pa · s - eegr E=1 value of viscosity atE=1, Pa · s - eegr * reduced viscosity, eq. (43), Pa · s - Lambda zero-residence-time rheological time constant, s - rhov density, kg/m3 - phiv(t),psgr(t) residence time functions
Keywords:Reactive polymer melt  rheometrical flow surface  polyamide-6
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