Method for producing naphthalene-based superplasticizer by using H acid wastewater recovered solution
A high-efficiency water-reducing agent and wastewater recycling technology, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc. problems, to achieve good economic and environmental benefits, protect the environment, and improve the effect of pollution
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Embodiment 1
[0027] Get 120mL of production waste water (pH=2, COD=20000mg / L, salt content=100g / L) of H acid-base fusion and acid analysis process, adopt the system of trialkylamine+octyl alcohol+kerosene as extraction agent, to H acid Production wastewater is extracted. Add H-acid production wastewater and 40ml extractant into a 250ml separatory funnel, shake for 20 minutes at room temperature and then let stand for 40 minutes to separate the organic phase and the aqueous phase. The obtained aqueous phase was subjected to multistage extraction by the same method as above, and the COD of the treated aqueous phase was 800 mg / L.
[0028] The obtained extract was transferred into a separatory funnel, and 18 ml of 20% sodium hydroxide solution was added for back extraction. After oscillating for 30 minutes at room temperature, stand still for 30 minutes to separate the extractant and back-extraction solution, the extractant is recycled, and the back-extraction solution is used to produce a wa...
Embodiment 2
[0031] Get 100mL of H acid separation T acid process production wastewater (pH=2, COD=38500mg / L, salt content=200g / L), adopt the system of trialkylamine+octyl alcohol+kerosene as extraction agent, to H acid production waste water for extraction. Add H-acid production wastewater and 30ml extractant into a 250ml separatory funnel, shake for 20 minutes at room temperature and then let stand for 40 minutes to separate the organic phase and the aqueous phase. The obtained aqueous phase was subjected to multi-stage extraction by the same method as above, and the COD of the treated aqueous phase was 1500 mg / L.
[0032] The obtained extract was transferred into a separatory funnel, and 10 ml of 20% sodium hydroxide solution was added for back extraction. After oscillating for 30 minutes at room temperature, stand still for 30 minutes to separate the extractant and back-extraction solution, the extractant is recycled, and the back-extraction solution is used to produce a water reducer...
Embodiment 3
[0035] Take 100mL of mixed waste water (pH=2, COD=30000mg / L, salt content=150g / L) from H acid-base fusion acid separation process and T acid separation process, and use the system of trialkylamine + sulfonated kerosene as the extraction agent , to extract H acid production wastewater. Add H-acid production wastewater and 30ml extractant into a 250ml separatory funnel, shake for 20 minutes at room temperature and then let stand for 40 minutes to separate the organic phase and the aqueous phase. The obtained aqueous phase was subjected to multistage extraction by the same method as above, and the COD of the treated aqueous phase was 1220 mg / L. After the water phase is decolorized by activated carbon, the salts therein can be recovered through concentrated crystallization.
[0036] The obtained extract was transferred into a separatory funnel, and 10 ml of 20% sodium hydroxide solution was added for back extraction. After oscillating for 30 minutes at room temperature, stand st...
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