Technology and system for improving yield of nitric acid regenerated by stainless steel acid-washing waste liquid
A technology for pickling waste liquid and stainless steel, which is applied in the fields of nitric acid, nitrogen oxides/oxyacids, water/sludge/sewage treatment, etc. Absorption rate, the effect of improving yield
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Embodiment 1
[0055] In this embodiment, the heat generated by natural gas combustion is used as the heat source to preheat the hydrolysis roaster 1, and then heated to the required temperature, wherein the furnace top temperature is 250°C, and the furnace bottom temperature is 650°C; the high-temperature flue gas enters the pre-concentrator In step 2, the pickling waste liquid is added to the pre-concentrator 2, and the pickling waste liquid is concentrated while cooling the high-temperature flue gas.
[0056] The composition of the processed stainless steel pickling waste liquor is as shown in table 1:
[0057] Table 1
[0058] Element
g / L
Ae (metal ion)
45
F ion
45
NO 3 -
145
total
235
[0059] Treat waste liquid 6m per hour 3 / h.
[0060] The composition of pickling waste liquid after pre-concentration in pre-concentrator 2 is shown in Table 2:
[0061] Table 2
[0062] Element
g / L
Ae (metal ion)
...
Embodiment 2
[0078] In this embodiment, the heat generated by natural gas combustion is used as the heat source to preheat the hydrolysis roaster 1, and then heated to the required temperature, wherein the furnace top temperature is 350°C, and the furnace bottom temperature is 750°C; the high-temperature flue gas enters the pre-concentrator In step 2, the pickling waste liquid is added to the pre-concentrator 2, and the pickling waste liquid is concentrated while cooling the high-temperature flue gas.
[0079] The composition of the processed stainless steel pickling waste liquor is as shown in table 6:
[0080] Table 6
[0081] Element
g / L
Ae (metal ion)
55
F ion
55
NO 3 -
165
total
280
[0082] Treat waste liquid 6m per hour 3 / h.
[0083] The composition of pickling waste liquid after pre-concentration in pre-concentrator 2 is shown in Table 7:
[0084] Table 7
[0085] Element
g / L
Ae (metal ion)
...
Embodiment 3
[0101] In this embodiment, the heat generated by natural gas combustion is used as the heat source to preheat the hydrolysis roaster 1, and then heated to the required temperature, wherein the furnace top temperature is 300°C, and the furnace bottom temperature is 700°C; the high-temperature flue gas enters the pre-concentrator In step 2, the pickling waste liquid is added to the pre-concentrator 2, and the pickling waste liquid is concentrated while cooling the high-temperature flue gas.
[0102] The composition of the processed stainless steel pickling waste liquor is as shown in table 11:
[0103] Table 11
[0104] Element
g / L
Ae (metal ion)
55
F ion
50
NO 3 -
150
total
255
[0105] Treat waste liquid 6m per hour 3 / h.
[0106] The composition of the pickling waste liquid after pre-concentration in the pre-concentrator 2 is shown in Table 12:
[0107] Table 12
[0108] Element
g / L
Ae (met...
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