Production process of blending type regeneration polyester flame retardant staple fiber
A recycled polyester and production process technology, which is applied in the manufacture of fire-resistant and flame-retardant filaments, the melting of single-component polyester artificial filaments, and filament raw materials, can solve the problems of complex process operations and high production costs, and achieve production Simple process, low production cost and good spinnability
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Problems solved by technology
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Examples
Embodiment 1
[0031] (1) Put 100kg of white recycled polyester bottle flakes into a drum for drying at 140°C, and at the same time put 5kg of phosphorus-based flame retardant in a constant temperature vacuum drying oven to dry at 80°C. When the moisture content of the fuel is below 50ppm, mix the recycled polyester bottle flakes with the phosphorus flame retardant evenly.
[0032] (2) Feed the mixture of recycled polyester bottle flakes and phosphorus-based flame retardant into the screw extruder of the spinning production line, heat and melt to form a melt, the melt passes through a filter, and is metered by a spinning pump at 8Mpa The pressure is ejected through the spinneret holes, and the speed at which the filaments are ejected from the spinneret holes is 1100-1400m / min (1100m / min in this embodiment), and the primary fibers are formed after cooling and solidification; the screw rods of the screw extruder are seven The heating temperatures of the zones are: 270-275°C, 275-280°C, 280-285...
Embodiment 2
[0038] (1) Put 100kg of white regenerated polyester bottle flakes into a drum for drying at 145°C, and at the same time put 12kg of phosphorus-based flame retardants into a constant temperature vacuum oven to dry at 85°C. When the moisture content of the fuel is below 50ppm, mix the recycled polyester bottle flakes with the phosphorus flame retardant evenly.
[0039] (2) Feed the mixture of recycled polyester bottle flakes and phosphorus-based flame retardant into the screw extruder of the spinning production line, heat and melt to form a melt, the melt passes through a filter, and is metered by a spinning pump at 10Mpa The pressure is ejected through the spinneret holes, and the speed at which the filaments are ejected from the spinneret holes is 1100-1400m / min (1400m / min in this embodiment), and the primary fibers are formed after cooling and solidification; the screw rods of the screw extruder are seven The heating temperatures of the zones are: 270-275°C, 275-280°C, 280-28...
Embodiment 3
[0045] (1) Put 100kg of white recycled polyester bottle flakes into a drum for drying at 142°C, and at the same time put 8kg of phosphorus-based flame retardant in a constant temperature vacuum drying oven to dry at 82°C. When the moisture content of the fuel is below 50ppm, mix the recycled polyester bottle flakes with the phosphorus flame retardant evenly.
[0046] (2) Feed the mixture of recycled polyester bottle flakes and phosphorus-based flame retardant into the screw extruder of the spinning production line, heat and melt to form a melt, the melt passes through a filter, and is metered by a spinning pump at 9Mpa The pressure is ejected through the spinneret holes, and the speed at which the filaments are ejected from the spinneret holes is 1100-1400m / min (1200m / min in this embodiment), and the primary fibers are formed after cooling and solidification; the screw rods of the screw extruder are seven The heating temperatures of the zones are: 270-275°C, 275-280°C, 280-285...
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Abstract
Description
Claims
Application Information
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