Production method of high-viscosity cotton pulp
A production method and cotton pulp technology, applied in pulp bleaching, pulp dehydration, pulping with inorganic alkali, etc., can solve the problems of temperature control gap, large difference in cooking pulp quality, long cooking cycle, etc., to achieve reasonable process and realize The effect of industrial mass production
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Embodiment 1
[0109] (1) According to the continuous feeding method, the cotton linters are fed into the cyclone semi-pulp machine through open cotton, secondary open cotton, dry cleaning system, cyclone separator, screw pressure screw; the current of the cyclone semi-pulp machine is controlled at 400A~ In the range of 430A, the fiber is cut in series, and the fiber length is controlled at 3mm~5mm to obtain the slurry and send it to the material preparation tank.
[0110] (2) The slurry prepared in step (1) is pumped into the oblique spiral through the sizing pump, and then pre-dewatered into the double-roll extruder through the oblique spiral. The slurry is dehydrated to 25% dryness and enters the return spiral to ensure the return spiral. In the case of a certain amount of return material, the single screw meter is turned on, and the slurry enters the screw conveyor according to the calculated air-dry mass of 3.3 tons / hour, and is continuously and uniformly sent to the feeder, and enters the ...
Embodiment 2
[0118] The production method provided in Example 1 is used to obtain high-viscosity cotton pulp. The difference is that the temperature of the first cooking tube in step (3) is 125°C to 126°C, and the rotational speed is 1.8r / min; the second cooking tube The temperature is 124.8℃~125.8℃, and the rotation speed is 1.7r / min; the temperature of the third cooking tube is 124.7℃~125.7℃, and the rotation speed is 1.6r / min; the mixed slurry moves at a speed of 0.43m / min The cooking is carried out sequentially through the above three cooking tubes.
[0119] After testing, the quality testing results of the high-viscosity cotton pulp provided in Example 2 of the present invention are:
[0120] Degree of polymerization is 2712; whiteness is 74.6%; dust ≤488mm 2 / 500g; the nail fiber is 99.7%; the iron is 8×10 -6 ; Ash content is 0.07%; meets the performance requirements of high-viscosity cotton pulp 2600 products.
Embodiment 3
[0122] The production method provided in Example 1 is used to obtain high-viscosity cotton pulp. The difference is that: in step (3), the temperature of the first cooking tube is 124°C to 125°C, and the rotational speed is 1.9r / min; the second cooking tube The temperature is 123.8℃~124.8℃, the rotation speed is 1.8r / min; the temperature of the third cooking tube is 123.7℃~124.7℃, the rotation speed is 1.7r / min; the mixed slurry moves at a speed of 0.46m / min The cooking is carried out sequentially through the above three cooking tubes.
[0123] After testing, the quality testing results of the high viscosity cotton pulp provided in Example 3 of the present invention are:
[0124] The degree of polymerization is 2736; the whiteness is 74.3%; dust ≤493mm 2 / 500g; nail fiber is 99.7%; iron is 9×10 -6 ; Ash content is 0.08%; meets the performance requirements of high-viscosity cotton pulp 2600 products.
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