Paper making black liquor recycling zero discharge process adopting rotary membrane treatment
A technology of papermaking black liquor and rotary type, which is applied in the regeneration of lye, etc., can solve the problems of operation, complicated operation, multiple procedures, and high technical requirements, and achieve low operating cost, short water intake process, and meet engineering requirements Effect
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example 1
[0027] Example 1: Treating papermaking black liquor wastewater COD=24000-30000mg / L with wheat straw as raw material
[0028] 20% calcium chloride solution is used, the acid solution is waste acid from the steel pipe factory, and the ultrafiltration membrane adopts polyvinylidene fluoride (PVDF) with a pore size of 0.02 μm. Specific operation: (1) Add 20% calcium chloride solution to the papermaking black liquor, adjust the pH value to 6, and the reaction time is 30 minutes, then add the waste acid from the steel pipe factory containing iron, adjust the pH value to 4, and the reaction time 30min, the removal rate of CODCr reached 90%, the removal rate of SS was about 85%, the removal rate of chroma was 95%, and the recovery rate of calcium lignin was about 80%. Solid-liquid separation, the obtained supernatant enters the Fenton strong oxidation system for further treatment, and the COD of the effluent after the Fenton strong oxidation treatment is reduced by less than 60 mg / L, ...
example 2
[0030] Example 2: Treating papermaking black liquor wastewater COD=15000-20000mg / L with rice straw as raw material
[0031] 20% calcium chloride solution is used, the acid solution is waste acid from the steel pipe factory, and the ultrafiltration membrane adopts polyvinylidene fluoride (PVDF) with a pore size of 0.02 μm. Specific operation: (1) Add 20% calcium chloride solution to the papermaking black liquor, adjust the pH value to 7, and the reaction time is 30 minutes, then add the waste acid from the steel pipe factory containing iron, adjust the pH value to 6, and the reaction time 30min, the removal rate of CODCr reached 90%, the removal rate of SS was about 85%, the removal rate of chroma was 95%, and the recovery rate of calcium lignin was about 80%. Solid-liquid separation, the obtained supernatant enters the Fenton strong oxidation system for further treatment, and the COD of the effluent after the Fenton strong oxidation treatment is reduced by less than 48 mg / L, r...
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