Continuous pretreatment method of maleic anhydride emulsifying waste water
A technology for emulsification of wastewater and maleic anhydride, applied in multi-stage water treatment, water/sewage treatment, natural water treatment, etc., can solve the problems of increased energy consumption, complex process and high production cost
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Embodiment 1
[0034] Preparation of the adsorbent:
[0035] The lignite is ground by a coal mill to obtain coal powder with a particle size of 15-30 μm. The raw material of diatomite is dried at 120°C and pulverized by high-pressure airflow. Coal powder and diatomaceous earth are ground and mixed according to the mass ratio of 9:1 to obtain the adsorbent.
[0036] Wastewater treatment process:
[0037] The COD 9500 in the supernatant liquid I obtained after the maleic anhydride emulsified wastewater was settled in the settling tank, the content of dibutyl phthalate was 0.15% (wt), and the supernatant liquid I was continuously added to the stirring adsorption tank at 500kg / h, and the adsorption The agent is continuously added into the stirring adsorption tank at a rate of 10kg / h through a feeder, and the residence time is controlled at 20min to obtain a mixed slurry. After the mixed slurry is separated by a solid-liquid separator, the separated solid is dried and incinerated. Add polyalu...
Embodiment 2
[0039] Preparation of the adsorbent:
[0040] The lignite is ground by a coal mill to obtain coal powder with a particle size of 15-30 μm. The raw material of diatomite is dried at 120°C and pulverized by high-pressure airflow. Coal powder and diatomaceous earth are ground and mixed in a mass ratio of 9:1.
[0041]Wastewater treatment process:
[0042] After the maleic anhydride emulsified wastewater settles in the settling tank, the COD is 16300, and the dibutyl phthalate content is 0.78% (wt). It is continuously added to the stirring adsorption tank at 500kg / h, and the adsorbent is continuously added at a speed of 40kg / h through the feeder. In the stirred adsorption tank, the residence time is controlled at 20min. The mixed slurry is separated by a solid-liquid separator for solid-liquid separation. After the mixed slurry is separated by a solid-liquid separator, the separated solid is dried and incinerated. Add polyaluminum sulfate to the obtained supernatant II, and th...
Embodiment 3
[0044] Preparation of the adsorbent:
[0045] The lignite is ground by a coal mill to obtain coal powder with a particle size of 1-15 μm. The raw material of diatomite is dried at 120°C and pulverized by high-pressure airflow. Coal powder and diatomaceous earth are ground and mixed in a mass ratio of 9:1.
[0046] Wastewater treatment process:
[0047] After the maleic anhydride emulsified wastewater settles in the settling tank, the COD is 16300, and the dibutyl phthalate content is 0.78% (wt). It is continuously added to the stirring adsorption tank at 500kg / h, and the adsorbent is continuously added at a speed of 40kg / h through the feeder. In the stirred adsorption tank, the residence time is controlled at 20min. The mixed slurry is separated by a solid-liquid separator for solid-liquid separation, and the separated solid is dried and incinerated. Add polyaluminum sulfate to the obtained supernatant II, and the feeding rate is 5g / h (the total amount of flocculant added ...
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