Melt Spinning

Melt Residence Time, Thermal History & IV Loss Risk

Thermal loss is an extruder problem. Hydrolytic loss was decided in the dryer.

Thermal History Where the melt has been and for how long
deg C
deg C
min
deg C

The temperature the equivalent time is expressed at

Kinetics & Moisture Rate constants for the polymer and the water it carried in
kJ/mol

PET main-chain scission is typically 100-140

dL/g/min
ppm
dL/g/ppm/min
dL/g

Predicted IV Loss

— dL/g

Thermal and hydrolytic scission combined

Rate, Split & Time Budget

Thermal Component
— dL/g
Hydrolytic Component
— dL/g
Hydrolytic Share of the Loss
— %
Equivalent Time at Reference
— min
Rate Ratio vs Reference
— x
Effective Melt Temperature
— deg C
Residence Time the Budget Allows
— min

Both mechanisms are treated as first order and independent, which is a simplification: hydrolysis is autocatalytic through the carboxyl end groups it generates, so a badly dried melt degrades faster as it goes and this will read low for high moisture. The single residence time is a mean, and the damage in a real machine is dominated by the tail of the distribution rather than the mean, so a machine with dead volume will lose more IV than this predicts while appearing correct on paper. The rate constants are grade-specific and must be calibrated against a measured chip-to-yarn IV pair before absolute predictions are trusted; the rate ratio and the equivalent time are far more transferable and are the outputs to rely on when comparing conditions. Thermo-oxidative degradation from air ingress at the hopper throat is not modelled and can dominate everything here if it is present.

Melt Residence Time, Thermal History & IV Loss Risk — free, with the formula and a worked example, at Textile School.