Method for extracting and refining potassium salt from mica acid production wastewater
A technology for producing wastewater and side-chain acids, which is applied in combustion methods, chemical instruments and methods, water/sewage treatment, etc., can solve problems such as low purity of potassium silicate, increase of harmful gas content in combustion tail gas, and high treatment costs, and achieve investment Low cost, less impurities, and high wastewater treatment efficiency
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Embodiment 1
[0031] 10t of cefixime side chain acid production wastewater is treated, and potassium chloride is extracted, and the potassium ion mass content of the detected wastewater is 7.8%, the calorific value is 82cal / g, and the pH value is 6.5, the method is as follows:
[0032] (1) Pretreatment: adopt the conventional concentration method to concentrate the waste water produced by cefixime side chain acid until the mass content of potassium ions is 18%, then add high calorific value wastewater (calorific value > 1000cal / g) until its calorific value reaches 500±50cal / g, then add waste potassium hydroxide until its pH value is 8±0.5;
[0033] (2) Incineration: The temperature of the high-temperature liquid incinerator is controlled at 900°C, the pretreated wastewater is sprayed into the high-temperature liquid incinerator for incineration, and the gas-solid separation is carried out through the cyclone separator and bag filter, and the generated gas is subjected to high temperature Af...
Embodiment 2
[0038] 5t of cefixime side chain acid production wastewater is treated, and potassium chloride is extracted, and the potassium ion mass content of the detected wastewater is 9.6%, the calorific value is 1130cal / g, and the pH value is 12.2, the method is as follows:
[0039] (1) Pretreatment: adopt the conventional concentration method to concentrate the waste water from the production of cefixime side chain acid until the mass content of potassium ions is 20%, and then add low calorific value wastewater (calorific value<100cal / g) until its calorific value reaches 900±100cal / g, then add waste hydrochloric acid until its pH value is 8±0.5;
[0040] (2) Incineration: The temperature of the high-temperature liquid incinerator is controlled at 600°C, the pretreated wastewater is sprayed into the high-temperature liquid incinerator for incineration, and the gas-solid separation is carried out through a cyclone separator and a bag filter. After denitrification, desulfurization, absor...
Embodiment 3
[0045] 10t of cefixime side chain acid production wastewater is treated, and potassium chloride is extracted, and the potassium ion mass content of the detected wastewater is 6.2%, the calorific value is 95cal / g, and the pH value is 5.3, the method is as follows:
[0046] (1) Pretreatment: Concentrate the waste water from the production of cefixime side chain acid by conventional concentration methods until the mass content of potassium ions is 15%, then add methanol until its calorific value reaches 200±50cal / g, and then add waste oxidation Potassium and waste potassium hydroxide to its pH value of 8 ± 0.5;
[0047] (2) Incineration: The temperature of the high-temperature liquid incinerator is controlled at 1200°C, the pretreated wastewater is sprayed into the high-temperature liquid incinerator for incineration, and the gas-solid separation is carried out through the cyclone separator and bag filter, and the generated gas is subjected to high temperature After denitrificati...
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