Application of methyl n-butyl ketone and treatment method of phenolic wastewater
A technology of methyl n-butyl ketone and treatment method, which is applied in the field of treatment of phenol-containing wastewater, and can solve problems such as inability to remove polyphenols well
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Embodiment 1
[0027] This embodiment is used to illustrate the treatment method of phenol-containing wastewater provided by the present invention.
[0028] Phenol-containing wastewater (total phenol content is 12700mg·L -1 , the unit phenol content is 8450mg·L -1 , the content of polyphenols is 4250mg·L -1 , COD value is 32268mg·L -1 ) to adjust the pH value to 6.5, and conduct countercurrent extraction with the dephenolizing extractant methyl n-butyl ketone in the extraction tower. The extraction temperature is 40°C, and the extract phase containing crude phenol and a large amount of dephenolizing extractant and the raffinate phase containing a small amount of dephenolizing extractant and a large amount of waste water are respectively obtained. The extraction phase enters the rectification tower, that is, the phenol tower. The theoretical stages of rectification are 15, the temperature of the tower bottom is 211-213°C, and the pressure is 0.105-0.11MPa. product. The raffinate phase en...
Embodiment 2
[0030] This embodiment is used to illustrate the treatment method of phenol-containing wastewater provided by the present invention.
[0031] Phenol-containing wastewater (total phenol content is 12700mg·L -1 , the unit phenol content is 8450mg·L -1 , the content of polyphenols is 4250mg·L -1 , COD value is 32268mg·L -1 ) to adjust the pH value to 8, and conduct countercurrent extraction with the dephenolizing extractant methyl n-butyl ketone in the extraction tower. The temperature is 85°C, and the extract phase containing crude phenol and a large amount of dephenolizing extractant and the raffinate phase containing a small amount of dephenolizing extractant and a large amount of waste water are respectively obtained. The extraction phase enters the rectification tower, that is, the phenol tower. The theoretical stages of rectification are 5, the temperature of the tower bottom is 218-220°C, and the pressure is 0.14-0.15MPa. product. The raffinate phase enters the rectif...
Embodiment 3
[0033] This embodiment is used to illustrate the treatment method of phenol-containing wastewater provided by the present invention.
[0034] Phenol-containing wastewater (total phenol content is 12700mg·L -1 , the unit phenol content is 8450mg·L -1 , the content of polyphenols is 4250mg·L -1 , COD value is 25145mg·L -1 ) to adjust the pH value to 5, and with the mixture of the dephenolic extractant methyl n-butyl ketone and methyl isobutyl ketone (based on the total weight of the mixture, the content of the methyl n-butyl ketone is 80 volume %, the content of the methyl isobutyl ketone is 20% by weight) in the extraction tower for countercurrent extraction, the extraction theoretical stage is 8, the volume of the dephenol extraction agent and the phenol-containing wastewater is 1:10, and the extraction temperature is 50 °C, the extract phase containing crude phenol and a large amount of dephenolizing extractant and the raffinate phase containing a small amount of dephenoli...
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