Wheat straw pulp black liquor alkali recovery method
A recovery method and black liquor caustic soda technology can be applied in the combustion of pulping waste liquid, regeneration of pulping liquid, and concentration of waste liquid, etc. The effect of organic dye load, reducing high-load pollution and reducing pollution load
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Embodiment 1
[0013] A method for recovering wheat straw pulp black liquor alkali, comprising the following steps:
[0014] 1) In the black liquor evaporation and concentration section, a five-effect full-plate evaporator is used to evaporate and concentrate the black liquor, and the evaporation intensity is 10kg water / m 2 h, concentration of thick black liquor after evaporation is 40%%; evaporation area of evaporator is 6200m 2 .
[0015] 2) The black liquor combustion section, the concentrated black liquor obtained in the above step 1) is further evaporated and concentrated by the disc evaporator using three winds, then enters the alkali furnace for cracking and combustion, and finally goes to the dissolution tank to make green liquor, and the alkali furnace The furnace temperature is 500°C, the furnace pressure is 0MPa, the primary and secondary air temperatures are 280°C, the primary air pressure is 600Pa, the secondary air pressure is 800Pa, and the third air pressure is 1000Pa;
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Embodiment 2
[0018] A method for recovering wheat straw pulp black liquor alkali, comprising the following steps:
[0019] 1) In the black liquor evaporation and concentration section, a five-effect full-plate evaporator is used to evaporate and concentrate the black liquor, and the evaporation intensity is 11kg water / m 2 h, concentration of thick black liquor after evaporation is 44%; evaporation area of evaporator is 6200m 2 .
[0020] 2) The black liquor combustion section, the concentrated black liquor obtained in the above step 1) is further evaporated and concentrated by the disc evaporator using three winds, then enters the alkali furnace for cracking and combustion, and finally goes to the dissolution tank to make green liquor, and the alkali furnace The furnace temperature is 600°C, the furnace pressure is 20MPa, the primary and secondary air temperatures are 290°C, the primary air pressure is 800Pa, the secondary air pressure is 1000Pa, and the third air pressure is 1500Pa;
...
Embodiment 3
[0023] A method for recovering wheat straw pulp black liquor alkali, comprising the following steps:
[0024] 1) In the black liquor evaporation and concentration section, a five-effect full-plate evaporator is used to evaporate and concentrate the black liquor, and the evaporation intensity is 10.5kg water / m 2 h, concentration of thick black liquor after evaporation is 40%~44%; evaporation area of evaporator is 6200m 2 .
[0025] 2) The black liquor combustion section, the concentrated black liquor obtained in the above step 1) is further evaporated and concentrated by the disc evaporator using three winds, then enters the alkali furnace for cracking and combustion, and finally goes to the dissolution tank to make green liquor, and the alkali furnace The furnace temperature is 550°C, the furnace pressure is 10MPa, the primary and secondary air temperatures are 285°C, the primary air pressure is 700Pa, the secondary air pressure is 900Pa, and the third air pressure is 1200P...
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