Method for treating and recycling molybdenum calcine water-washing waste water
A technology for waste water treatment and molybdenum calcining, applied in the direction of flocculation/sedimentation water/sewage treatment, etc., can solve the problems of environmental protection, long treatment period, frequent membrane cleaning, difficult regeneration, etc., achieving less consumables, small equipment investment, and simple operation. Effect
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Embodiment 1
[0020] The pH value of the molybdenum calcine washing wastewater in this embodiment is 3-4, and the concentration of each ion in the wastewater is: molybdenum 24.29g / L, copper 0.5g / L, iron 0.74g / L, potassium 0.8g / L, sodium 0.028g / L, calcium 0.21g / L, magnesium 0.35g / L; acid precipitation crystallization mother liquor pH value is 5, each ion index is: molybdenum 15.74g / L, copper 0.004g / L, iron 0.0026g / L, potassium 0.076g / L, sodium 0.17g / L, calcium 0.015g / L, magnesium 0.024g / L.
[0021] The method that the molybdenum calcined sand washing waste water of the present embodiment is treated and recycled is:
[0022] Step 1, mix the molybdenum calcination wastewater with the acid precipitation crystallization mother liquor in the ammonium molybdate production process in a volume ratio of 1: 2.5 and stir evenly, then use nitric acid (also can be replaced by other acids) to adjust the pH value to 2.5, continue Stir for 30min to obtain a solid-liquid mixture;
[0023] Step 2, adopt p...
Embodiment 2
[0025] The filter cake that embodiment 1 is obtained is sent into the ammonium molybdate production process and carried out conventional ammonia leaching process; The roasted molybdenum concentrate is pickled, the pickling temperature is 90°C, the pH value is 0.5-1, the liquid-solid ratio (the mass ratio of the filtrate to the roasted molybdenum concentrate) is 3:1, and the pickling time is 1h Then adopt plate and frame filter press to carry out solid-liquid separation to the slurry after pickling treatment, the filter cake obtained by separation is sent into the ammonia leaching operation of ammonium molybdate production process to carry out ammonia leaching treatment, and the filtrate obtained by separation is sent to into the wastewater treatment system and then discharged after reaching the standard.
[0026] The mass content of molybdenum in the roasted molybdenum concentrate of the present embodiment is 63.03%, the mass content of copper is 0.13%, and the mass content of...
Embodiment 3
[0028] The pH value of the molybdenum calcine washing wastewater in this embodiment is 3-4, and the concentration of each ion in the wastewater is: molybdenum 26.64g / L, copper 0.96g / L, iron 0.029g / L, potassium 0.68g / L, sodium 0.027g / L, calcium 0.026g / L, magnesium 0.03g / L; acid precipitation crystallization mother liquor pH value is 2.5, each ion index is: molybdenum 15g / L, copper 0.016g / L, iron 1.52g / L, potassium 0.056g / L L, sodium 0.15g / L, calcium 0.24g / L, magnesium 0.34g / L.
[0029] The method that the molybdenum calcined sand washing waste water of the present embodiment is treated and recycled is:
[0030] Step 1, mix the molybdenum calcination wastewater with the acid precipitation crystallization mother liquor in the ammonium molybdate production process at a volume ratio of 1:0.5 and stir evenly, then adjust the pH value to 1.0 with nitric acid (also can be replaced by other acids), continue Stir for 60min to obtain a solid-liquid mixture;
[0031] Step 2, adopt plat...
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