Abstract Process for improving the production efficiency of the spinning of an undrawn, preoriented yarn based on polyethylene terephthalate (PET) by the introduction, before the spinning, of 0.03 to 0.1% by weight of fumed silica with a particle size of between 5 and 15 nm into the molten polymer in the form of dispersion in a masterbatch of the same polymer as that to be processed, then spinning the PET containing the silica in the finely dispersed state, the filaments being next cooled by means of a gas stream at temperature between 17 DEG to 22 DEG C. and then sized and wound at a velocity of between 3500 and 5000 m/min. The gain in production efficiency, evaluated in relation to the shrinkage of the filaments in dry air at 180 DEG C., is at least 7%, generally at least 10-15%.
Process for improving the production efficiency during the spinning of an undrawn, preoriented yarn based on polyethylene terephthalate (PET) at a velocity of at least 3000 m/min, characterized in that, before the spinning, 0.03 to 0.1% by weight of fumed silica with a particle size of between 5 and 15 nm is introduced into the molten polymer in the form of dispersion in a masterbatch of the same polymer as that to be processed, followed by spinning of the PET containing the silica in the finely dispersed state, the filaments being next cooled by means of a gas stream at temperature between 17° to 22° C. and then sized and wound at a velocity of between 3500 and 5000 m/min.
Claim 2
Dependent Claim
120 words
Process for improving the production efficiency during the spinning of an undrawn, preoriented yarn based on polyethylene terephthalate (PET) at a velocity of at least 3000 m/min, characterized in that, before the spinning, 0.03 to 0.1% by weight of fumed silica with a particle size of between 5 and 15 nm is introduced into the molten polymer in the form of dispersion in a masterbatch of the same polymer as that to be processed, followed by spinning of the PET containing the silica in the finely dispersed state, the filaments being next cooled by means of a gas stream at temperature between 17° to 22° C. and then sized and wound at a velocity of between 3500 and 5000 m/min.
Claim 3
Dependent Claim
22 words
Process according to claim 1, characterized in that the fumed silica is introduced in a proportion of 0.05 to 0.1% by weight.
Claim 4
Dependent Claim
31 words
Process according to claim 1, characterized in that the gain in production efficiency, evaluated in relation to the dry air shrinkage of the filaments at 180° C. is at least 7%.
Claim 5
Dependent Claim
18 words
Process according to claim 1, characterized in that the improvement in production efficiency is of at least 10%.
Claim 6
Dependent Claim
22 words
Process according to claim 1, characterized in that the spinning is carried out at a velocity of between 4000 and 5000 m/min.
Claim 7
Dependent Claim
15 words
Process according to claim 1, characterized in that the filaments are interlaced before being wound.