PET bottle flake regeneration functional fiber production technology
A technology of functional fiber and production process, applied in the field of production process of PET bottle flakes regenerated functional fiber, can solve the problems of uneven product quality, energy waste, difficulty in grasping various indicators, etc.
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Embodiment 1
[0026] The production process of PET bottle flake recycled functional fiber, its production steps are as follows:
[0027] a). Firstly, pre-treat the PET bottle, remove the label, and then crush the waste PET bottle into a size of ≦30 PET bottle flakes; the broken bottle flakes are subjected to alkali washing; the alkali washing temperature is 90~95°C; after alkali washing, the non-PET bottle caps are removed by floating and sinking method;
[0028] b). Dry the PET bottle flakes obtained in step a by means of centrifugal negative pressure, so that the water content is 120-135ppm, and obtain PET low-viscosity primary material;
[0029] c). Increase the viscosity of the low-viscosity PET raw material obtained in step b, and increase the viscosity of the low-viscosity PET raw material obtained in step b at 180°C to make the viscosity reach 1.2~1.5ppm to obtain a high-viscosity PET raw material ; PET high-viscosity initial material and PET low-viscosity initial material are mixed...
Embodiment 2
[0038] a) First, pre-treat the PET bottle, remove the label from the PET bottle, and then crush the waste PET bottle into ≦30 PET bottle flakes; the broken bottle flakes are subjected to alkali washing; the alkali washing temperature is 90~95°C; after alkali washing, the non-PET bottle caps are removed by floating and sinking method;
[0039] b). Dry the PET bottle flakes obtained in step a by means of centrifugal negative pressure, so that the water content is 120-135ppm, and obtain PET low-viscosity primary material;
[0040] c). Thickening the PET low-viscosity primary material obtained in step b, and increasing the viscosity of the PET low-viscosity primary material obtained in b-step at 180°C to make the viscosity reach 1.2~1.5ppm to obtain a high-viscosity primary material; Mix the high-viscosity primary material and the low-viscosity primary material to obtain the target viscosity PET material; the mass parts of the high-viscosity primary material and the low-viscosity ...
Embodiment 3
[0049] a) First, pre-treat the PET bottle, remove the label from the PET bottle, and then crush the waste PET bottle into ≦30 PET bottle flakes; the broken bottle flakes are subjected to alkali washing; the alkali washing temperature is 90~95°C; after alkali washing, the non-PET bottle caps are removed by floating and sinking method;
[0050] b). Dry the PET bottle flakes obtained in step a by means of centrifugal negative pressure, so that the water content is 120-135ppm, and obtain PET low-viscosity primary material;
[0051] c). Thickening the PET low-viscosity primary material obtained in step b, and increasing the viscosity of the PET low-viscosity primary material obtained in b-step at 180°C to make the viscosity reach 1.2~1.5ppm to obtain a high-viscosity primary material; Mix the high-viscosity primary material and the low-viscosity primary material to obtain the target viscosity PET material; the mass parts of the high-viscosity primary material and the low-viscosity ...
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