Method for hybrid giant napier producing in oxygen free radical doffing/bleaching integrated reactor with dried bananas stalk
A technology of dried banana stems and free radicals, applied in pulp beating/refining method, bleaching agent addition, pretreatment with oxygen-generating compounds, etc., can solve the problems of low yield, large consumption of chemicals, environmental pollution, etc.
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Embodiment 1
[0053] A method for producing bleached pulp in an oxygen free radical removal / bleaching integrated reaction kettle for dry banana stems, comprising the following steps:
[0054] The dry banana stems sent from the material preparation section are sent to the material preparation room by the conveyor belt for pretreatment; washed and dehydrated with 60 ° C deionized water; the slurry is input into the oxidation reaction kettle with a screw conveyor, the model is M-O·P-II, and the concentration is added. 0.1% dimethyl sulfoxide; start the rotating electron accelerator and electric stirrer, the stirring speed is 1m / s, and the softening material stabilizes at 130°C; after opening the nitrogen gas for 3 minutes, open the pre-prepared composite oxygen pressure valve , under 0.6MPa oxygen pressure, adding concentration is 0.01% magnesium sulfate, 0.12% sodium silicate and concentration is 0.45% (H 2 o 2 ) cellulose hydrogen peroxide protective agent, 0.01% ethylenediaminetetraacetic ...
Embodiment 2
[0056] Same as Example 1, the difference is that the raw material is plantain fiber, and the oxidation reactor model is M-O·P-III type; it is washed and dehydrated with 80°C deionized water; the stirring speed is 0.8m / s; the stable temperature of the softened material is 140°C; Add concentration of 0.06% ferric oxide and 0.4% hydrogen peroxide (H 2 o 2 ) cellulose protective agent, a sodium polyphosphate oxygen stabilizer with a concentration of 0.3%, and a sodium percarbonate oxygen stabilizer with a concentration of 0.4%; react for 60min, and the pH value is 4; use a pulp washer in 80°C deionized water The pulp is repeatedly washed two to three times, dehydrated and left to stand, and stored in deionized water containing 0.01% N,N-dibenzylhydroxylamine to obtain a pulp with a pulp yield of 70% and a whiteness of 77.8% ISO.
Embodiment 3
[0058]Same as Example 1, the difference is that the raw material is pineapple fiber, and the oxidation reactor model is M-O·P-III type; it is washed and dehydrated with 80°C deionized water; the stirring speed is 0.8m / s; the stable temperature of the softened material is 120°C; Add concentration of 0.02% ferric oxide and 0.38% hydrogen peroxide (H 2 o 2 ) cellulose protective agent, sodium polyphosphate oxygen stabilizer with a concentration of 0.25%, and sodium percarbonate oxygen stabilizer with a concentration of 0.45%; react for 60 minutes, and have a pH value of 4.5; use a pulp washer in 80°C deionized water The pulp is repeatedly washed two to three times, dehydrated and left standing, and stored in deionized water containing 0.01% N,N-dibenzylhydroxylamine to obtain a pulp with a pulp yield of 68% and a whiteness of 76.5% ISO.
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