Method for harmless and recycling treatment of stainless steel acid washing waste water neutralization sludge
A technology for pickling wastewater and stainless steel, applied in water/sludge/sewage treatment, sludge treatment, chemical instruments and methods, etc. The effect of good effluent quality, high recovery efficiency and short process flow
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Embodiment 1
[0028] The neutralized sludge of stainless steel pickling wastewater was taken from a stainless steel pickling wastewater sewage treatment plant in Yancheng City, and the metal content in it was measured by digestion as follows:
[0029] element
Fe
mn
Ni
Cr
Content (mg / kg)
189924
4186
55406
8719
[0030] 1) Leaching: Dry the neutralized sludge of stainless steel pickling wastewater for 24 hours, and pass through a 60-mesh sieve after grinding to obtain powdery sludge. Mix 400g of sludge and 1600mL of water in a 2L beaker, add 1+1 sulfuric acid ( A total of 180mL) to maintain pH 1.0-1.5, leaching at room temperature for 1.5 hours. Obtain 1520mL of leach solution, the concentration of each metal element in the leach solution and the leaching rate are as follows:
[0031] element
Fe
mn
Ni
Cr
Concentration (mg / L)
27989
1082
14435
2260
56%
98.2%
99%
98.5% ...
Embodiment 2
[0037] The neutralized sludge of stainless steel pickling wastewater was taken from a stainless steel pickling wastewater sewage treatment plant in Yancheng City, and the metal content in it was measured by digestion as follows:
[0038] element
Fe
mn
Ni
Cr
Content (mg / kg)
113309
7068
6101
15610
[0039] 1) Leaching: Dry the neutralized sludge of stainless steel pickling wastewater for 24 hours, and pass through a 60-mesh sieve after grinding to obtain powdery sludge. Mix 400g of sludge and 1600mL of water in a 2L beaker, add 1+1 sulfuric acid ( A total of 160mL) to maintain the pH value of 1.0-1.5, leaching reaction for 1.5 hours. Obtain 1500mL of leach solution, the concentration of each metal element in the leach solution and the leaching rate are as follows:
[0040] element
Fe
mn
Ni
Cr
Concentration (mg / L)
18734
1838
1614
4038
62%
97.5%
99.2%
97%
...
Embodiment 3
[0046] The sludge was in the same batch as in Example 1. During the iron removal process, the pH value was controlled to be 4.0-4.5, the iron removal cycle was reduced to about 20 minutes, and the chromium loss rate rose to 17.6%. The oxidation process is the same as in Example 1, with a treatment capacity of 47BV. Recover nickel process with embodiment 1.
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