A resource treatment system and method for molybdenum-containing low-concentration nh4cl wastewater
A treatment system and low-concentration technology, applied in water/sewage treatment, chemical instruments and methods, neutralized water/sewage treatment, etc., can solve the problems of large consumption of chemicals and energy, unstable operation, high material requirements, etc., to achieve unlimited The effect of secondary pollution and low operating cost
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Embodiment 1
[0055] Ammonium chloride wastewater containing Mo in a factory (Mo content is 150mg / L, NH 4 Cl content is 0.1%), wastewater pH=3.5.
[0056] (1) Take 100L of the above wastewater, and add sodium hydroxide to the pH adjustment tank 1 to adjust the pH to 10;
[0057] (2) The wastewater coming out of the first pH adjustment tank first passes through the filter to remove possible precipitates, and then enters the hydrophobic membrane module for deamination, using 50L, 1% HCl as the ammonia absorption solution, and the ammonia nitrogen concentration is reduced to below 7ppm;
[0058] (3) The deaminized wastewater from the hydrophobic membrane module enters the sulfidation sedimentation tank, and n(Mo:Na 2 S) = 1:1 sodium sulfide as precipitant; 0.2% ammonium chloride absorption solution from the hydrophobic membrane module enters the first set of bipolar membrane for acid-base regeneration, and 0.1% to 1% ammonia water and 1% ~1.6% hydrochloric acid;
[0059] (4) The wastewater ...
Embodiment 2
[0064] Ammonium chloride wastewater containing Mo in a factory (Mo content is 1000mg / L, NH 4 Cl content is 2%), wastewater pH=7.
[0065] (1) Take 100L of the above wastewater, and add sodium hydroxide to the first pH adjustment tank to adjust the pH to 11;
[0066] (2) The wastewater from the first pH adjustment tank first enters the filter to remove possible precipitates, and then enters the hydrophobic membrane module for deamination, using 50L, 2% HCl as the ammonia absorption solution, and the ammonia nitrogen concentration is reduced to below 1ppm;
[0067] (3) The deaminated wastewater from the hydrophobic membrane module enters the sulfidation sedimentation tank, and n (Mo: Na 2 S) = 1:2 sodium sulfide as precipitant; 4% ammonium chloride absorption solution from hydrophobic membrane module enters the first set of bipolar membrane device for acid-base regeneration, and 0.5% to 3% ammonia water and 2 %~6% hydrochloric acid;
[0068] (4) The wastewater from the sulfid...
Embodiment 3
[0073] Ammonium chloride wastewater containing Mo in a factory (Mo content is 3500mg / L, NH 4 Cl content is 6%), wastewater pH=6.
[0074] (1) Take 100L of the above wastewater, and add sodium hydroxide to the first pH adjustment tank to adjust the pH to 10;
[0075] (2) The wastewater coming out of the first pH adjustment tank first passes through the filter to remove possible precipitates, and then enters the hydrophobic membrane module for deamination, using 50L of 5% HCl as the ammonia absorption solution, and the ammonia nitrogen concentration is reduced to below 5ppm;
[0076] (3) The deaminized wastewater from the hydrophobic membrane module enters the sulfidation sedimentation tank, and n(Mo:Na 2 S) = 1:2 sodium sulfide as precipitant; 10% ammonium chloride absorption solution from hydrophobic membrane module enters the first set of bipolar membrane for acid-base regeneration, and 3% to 6% ammonia water and 5% ammonium chloride can be obtained ~10% hydrochloric acid; ...
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