Comprehensive treatment and resource utilization method for industrial organic phosphorus waste liquid
A comprehensive treatment and organic phosphorus technology, applied in chemical instruments and methods, multi-stage water/sewage treatment, neutralized water/sewage treatment, etc., can solve the problems of secondary pollution, difficult to achieve standard discharge, etc., to reduce environmental pressure , The effect of reducing the generation of three wastes
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Embodiment 1
[0043] Mother liquor pretreatment:
[0044] Take the IDA route to synthesize diglyphosate waste liquid (containing 2.5% phosphorus and 1.1% nitrogen), and use a loaded activated carbon catalyst for catalytic wet oxidation, and detect the phosphate radicals in the oxidized waste liquid (calculated as orthophosphoric acid 7.88%, the same below ), the organic phosphorus conversion rate is 99.71%. Adjust the pH to 8.6, then concentrate through five-effect evaporation, and remove part of the separated sodium chloride solid at the same time. Obtain the concentrated solution containing 33.1% of phosphate, 2.31% of nitrate (calculated as nitric acid, the same below), 3.5% of chloride ion, and 16.5% of sodium ion.
[0045] Add a certain amount of ammonia to the concentrated solution after the above pretreatment to make the molar ratio of nitrate and ammonia reach 1 / 1, and then add solid sodium hydroxide to make the sodium ions and phosphate after deducting the sodium ions contained in...
Embodiment 2
[0048] Add a certain amount of ammonia to the concentrated solution after the pretreatment of the above-mentioned embodiment 1 to make the molar ratio of nitrate and ammonia reach 1 / 1, then add solid sodium hydroxide to make the sodium ion after deducting the sodium ion contained in the sodium chloride The molar ratio with phosphate reaches 2 / 1. Then the prepared concentrated mother liquor is atomized and sprayed into the fluidized bed drying and polycondensation device, the temperature in the fluidized bed is controlled at 350-500°C, and the average residence time is 25 minutes. The tail gas passes through the cyclone separator, waste heat boiler, and bag dust removal. Empty the device and so on. The fly ash collected by the cyclone separator and its bag filter is circulated to the fluidized bed drying polycondensation device. The solid was obtained at the bottom of the fluidized bed, and after analysis, the content of sodium pyrophosphate was 86.6%, sodium chloride was 11.2...
Embodiment 3
[0051] Add a certain amount of ammonia to the concentrated solution after the pretreatment of the above-mentioned embodiment 1 to make the molar ratio of nitrate and ammonia reach 1 / 1, then add an appropriate amount of phosphoric acid to make the sodium ion and phosphoric acid after deducting the sodium ion contained in sodium chloride The molar ratio of roots reaches 1.65 / 1. Then the prepared concentrated mother liquor is atomized and sprayed into the fluidized bed drying and polycondensation device, the temperature in the fluidized bed is controlled at 400-500°C, and the average residence time is 25 minutes. The tail gas passes through the cyclone separator, waste heat boiler, and bag dust removal. Empty the device and so on. The fly ash collected by the cyclone separator and its bag filter is circulated to the fluidized bed drying polycondensation device. The solid was obtained at the bottom of the fluidized bed. After analysis, the content of sodium polyphosphate was 88.2...
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