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Extruder operation startup

At the startup of the line, the extruder was operated at 91 rpm to produce the required rate of 148 kg/h for a specific rate of 1.63 kg/(h-rpm). The temperature of the extrudate was measured through the transfer line wall at 232 °C. Due to process safety constraints the extrudate temperature could not be measured using a handheld temperature sensor. The extrusion rate was required in order to maintain the downstream take-away equipment at its maximum rate. At first the extruder appeared to be operating well except that the specific rate was lower than predicted. That is, the screw was rotated at an rpm that was higher than expected to produce the 148 kg/h. At 91 rpm, the rotational flow rate was calculated at 228 kg/h the specific rotational flow rate was calculated at 2.51 kg/(h-rpm). Thus, the line was operating at only 65% of the rotational flow rate. A barrier design... [Pg.502]

This operation requires the personal skill of the startup person. That person is required to integrate/interrelate extruder and down-stream equipment. Extruder screw speeds and haul-off rates may then be increased. Downstream equipment is adjusted to meet their maximum operating performance, such as having the vacuum tank water operate with its proper level and vacuum applied. The extruder can be fine-tuned to obtain the final required setting for meeting the desired output rate and product size. [Pg.241]


See other pages where Extruder operation startup is mentioned: [Pg.251]    [Pg.251]    [Pg.258]    [Pg.258]    [Pg.266]    [Pg.549]    [Pg.251]    [Pg.251]    [Pg.258]    [Pg.258]    [Pg.266]    [Pg.549]    [Pg.262]    [Pg.345]    [Pg.361]    [Pg.501]    [Pg.181]    [Pg.468]    [Pg.480]    [Pg.495]    [Pg.552]    [Pg.630]    [Pg.238]    [Pg.242]    [Pg.260]    [Pg.200]    [Pg.256]    [Pg.410]    [Pg.481]    [Pg.161]    [Pg.385]    [Pg.287]   
See also in sourсe #XX -- [ Pg.251 ]




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EXTRUDER OPERATION

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Startup

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