Method for recycling heavy metal resources of stainless steel pickling waste water neutralization sludge
A technology of pickling wastewater and resource recovery, applied in chemical instruments and methods, water/sludge/sewage treatment, sludge treatment, etc., can solve the problems of complexity, low recovery rate of nickel and chromium, and achieve low loss of nickel and chromium , high recovery efficiency, good recovery effect
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Embodiment 1
[0028] The neutralized sludge of stainless steel pickling wastewater in this example comes from a sewage treatment plant in a stainless steel industrial park in Dafeng, Jiangsu. The sludge is obtained by treating stainless steel pickling wastewater with calcium chloride, lime and PAM. The main metal ion content is shown in Table 1. shown.
[0029] Table 1 Main metal ion content of stainless steel pickling wastewater and sludge in Example 1
[0030] element Fe mn Ni Cr Content g / kg 157.2 2.8 30 23.3
[0031] A kind of stainless steel pickling wastewater neutralization sludge heavy metal resource recovery method of the present embodiment, its specific steps are:
[0032] (1) Acid leaching: Take 40 g of the above sludge into a 500 mL three-neck flask, add 200 mL of water, stir evenly, add 80% sulfuric acid dropwise until the pH is stable at about 2.0, leaching for 50 min, then warming up to 95 °C, and then Add 8 mL, 360 g / L Na 2 SO 4 Solution (in...
Embodiment 2
[0037] The sludge and basic steps used in this example are the same as those in Example 1, except that in step (1), 90% sulfuric acid is added dropwise until the pH is stable at about 2.5, and after leaching for 10 min, the temperature is raised to 85°C, and then Na 2 SO 4 solution (in this example, the mass ratio of dry sludge to sodium sulfate is 5:1), put the three-necked flask in a water bath at 85°C, and keep stirring, then add jarosite crystal seeds (the dosage of the seed crystals is 10g / L), while adding 10% Na 2 CO 3 The pH value of the solution was controlled at 2.5, and after the iron removal reaction of jarosite was carried out for 5 h, 10% Na 2 CO 3 , adjust and control the pH value to 3.5, and add goethite seed crystals (the dosage of the seed crystals is 1 g / L), carry out the goethite reaction, and continue to react for 5 h. Increasing the pH is beneficial to inhibit the leaching of iron, but it will As a result, the leaching rate of nickel and chromium decre...
Embodiment 3
[0039] The sludge and basic steps used in this example are the same as in Example 1, the difference is that in step (1), 50% sulfuric acid is added dropwise until the pH is stable at 1.0, after leaching for 80 min, the temperature is raised to 75°C, and then Na 2 SO 4 solution (the mass ratio of dry sludge to sodium sulfate in this example is 25:1), put the three-necked flask in a 75°C water bath, and keep stirring, then add jarosite crystal seeds (the dosage of the seed crystals is 1 g / L), while adding 10% Na 2 CO 3 The pH value of the solution was controlled at 1.5, and after the iron removal reaction of jarosite was carried out for 1 h, 10% Na 2 CO 3 , adjust and control the pH value to 2.5, and add goethite seed crystals (the dosage of the seed crystals is 10 g / L), carry out the goethite reaction, and continue the reaction for 1.0 h; take 200mL in step (2) and step (1) Add potassium permanganate according to 130% of the amount required for the theoretical oxidation of ...
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