Method for reducing AOX forming amount in chlorine dioxide bleaching process of bagasse pulp
A technology of chlorine dioxide and bagasse pulp, which is applied in pulp bleaching, post-treatment of cellulose pulp, textiles and papermaking, etc., can solve the problems of extra input cost and unsatisfactory input-output ratio, etc., to reduce AOX and save Usage amount, effect of reducing pollution
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Embodiment 1
[0021] Method for reducing AOX formation in chlorine dioxide bleaching process
[0022] The washed and screened unbleached bagasse pulp is first sent to the pretreatment bleaching tower for two-stage pretreatment with high-temperature acid and enzyme, and then bleached with chlorine dioxide. The technological conditions of the high-temperature acid pretreatment section are: bleaching temperature 90°C, acid dosage 20kg / t 浆 , The reaction time is 60min. The unbleached pulp with a pulp concentration of 10% is preheated to 90°C and fully mixed with the acid solution in the slurry mixer, and then enters the pretreatment tower to start the reaction. The technological conditions of the biological enzyme pretreatment section are: bleaching temperature 60°C, enzyme dosage 20IU / g 浆 , The reaction time is 120min. After the slurry sprayed out from the high-temperature acid pretreatment tower is washed, the slurry concentration is adjusted to 10%, the reaction pH is controlled to be 6-9...
Embodiment 2
[0025] Method for reducing AOX formation in chlorine dioxide bleaching process
[0026] The washed and screened unbleached bagasse pulp is first sent to the pretreatment bleaching tower for two-stage pretreatment with high-temperature acid and enzyme, and then bleached with chlorine dioxide. The technological conditions of the high-temperature acid pretreatment section are: bleaching temperature 95°C, acid dosage 30kg / t 浆 , The reaction time is 75min. The unbleached pulp with a pulp concentration of 11% is preheated to 95°C and fully mixed with the acid solution in the slurry mixer, and then enters the pretreatment tower to start the reaction. The technological conditions of the biological enzyme pretreatment section are: bleaching temperature 75°C, enzyme dosage 30IU / g 浆 , The reaction time is 120min. After the slurry sprayed from the high-temperature acid pretreatment tower is washed clean, the slurry concentration is adjusted to 11%, the reaction pH is controlled to be 6...
Embodiment 3
[0029] Method for reducing AOX formation in chlorine dioxide bleaching process
[0030] The washed and screened unbleached bagasse pulp is first sent to the pretreatment bleaching tower for two-stage pretreatment with high-temperature acid and enzyme, and then bleached with chlorine dioxide. The technological conditions of the high-temperature acid pretreatment section are: bleaching temperature 98°C, acid dosage 50kg / t 浆 , The reaction time is 90min. The unbleached pulp with a pulp concentration of 15% is preheated to 98°C and fully mixed with the acid solution in the slurry mixer, and then enters the pretreatment tower to start the reaction. The technological conditions of the biological enzyme pretreatment section are: bleaching temperature 80°C, enzyme dosage 50IU / g 浆 , The reaction time is 120min. After the slurry sprayed out from the high-temperature acid pretreatment tower is washed, the slurry concentration is adjusted to 15%, the reaction pH is controlled to be 6-9...
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