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TOOLED THICK COMPOSITES by ARVEN H. SAUNDERS III ...

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Artificial neural networks have also been used to estimate reaction rate, as for example<br />

<strong>by</strong> Lee and Rice (Lee, 1997). A neural net is “trained” <strong>by</strong> learning the input-output relationships<br />

based on large amounts of known data. During training, the network adjusts its weights or<br />

coefficients that link each neuron in the network, so that the output is correctly predicted from<br />

the inputs. Backward propagation is a technique where errors in the input-output mapping are<br />

fed backwards, from output to inputs, to correct the weights. The neural network model of Lee et<br />

al predicts the reaction rate given the temperature and degree-of-cure inputs.<br />

Other researchers have developed other useful model forms. Ng (Ng, 1999) developed<br />

a 3rd order model that worked well with isothermal 8552 data. Shin et al (Shin, 2000) presented<br />

a new technique for applying to an autocatalytic model that more accurately predicts the final<br />

degree of cure. Costa et al (Costa, 2005) characterized carbon/epoxy 8552 using DSC and<br />

rheometer data, as well as dynamic mechanical analysis (DMA) to develop cure kinetics (nth<br />

order) and viscosity models<br />

In order to apply a cure model to an actual laminate, the material properties that affect<br />

the heat distribution must be accounted for. A commonly used formulation for estimating cure<br />

within a laminate is based on the “thermal-chemical” model first proposed <strong>by</strong> Loos and Springer<br />

(Loos, 1983). This model computes the temperature <strong>by</strong> laminate thickness position as a<br />

function of time. The Loos-Springer model is based on the solution of a one-dimensional heat<br />

conduction problem with internal heat generation. The governing partial differential equation is:<br />

2<br />

∂T<br />

K ∂ T 1<br />

= 2 +<br />

∂t ρC<br />

∂x<br />

C<br />

12<br />

dα<br />

H u<br />

dt<br />

where T is the temperature, t is the time, x is the through the thickness position, ρ is the density,<br />

C is the specific heat, K is the thermal conductivity, and Hu(dα/dt) is the rate of heat generated<br />

<strong>by</strong> the curing reaction. The boundary conditions are the upper and lower laminate surface<br />

temperatures which vary with time. The initial conditions are the temperature distribution, To(x),<br />

and degree-of-cure, αo(x), inside the laminate at the start of the process. The partial differential

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