A comprehensive recycling method for nitrogen-containing and sulfur-containing iron salt
A technology for iron salts and denitrification, applied in the fields of nitrogen compounds, chemical instruments and methods, ammonia compounds, etc., can solve the problems of inability to realize recycling, decline in direct metal yield, environmental pollution, etc., and achieve harmlessness and cleanliness. The effect of chemical treatment, easy control of technical conditions and short process flow
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Embodiment 1
[0016] The composition (mass percentage) of nitrogen-containing and sulfur-containing iron salt in this embodiment is: Fe 30%, SO 4 2- 45%, NO 3 - 5%;
[0017] Take 100 g of the above-mentioned nitrogen-containing and sulfur-containing iron salt, and denitrify at 450° C. for 1.0 h to obtain flue gas containing nitrogen oxides and 93 g of sulfur-containing iron salt. Flue gas containing nitrogen oxides is recovered for the production of nitric acid; the composition (mass percentage) of sulfur-containing iron salt is: Fe 32.81%, SO 4 2- 48.87%, NO 3 - 4 2- 0.11%, NO 3 - 0.04%, yield 57.30%; the solution composition after ammonia leaching is SO 4 2- 97.39 g / L, NO 3 - 4 + 43.98 g / L. The ammonia immersion solution is evaporated and crystallized to obtain ammonium sulfate crystals and condensed water. The contents of impurity elements Fe and Ni in ammonium sulfate crystals are less than 0.001%, which are exported directly and condensed water is recycled. The...
Embodiment 2
[0019] The composition (mass percentage) of nitrogen-containing and sulfur-containing iron salt in this embodiment is: Fe 50%, SO 4 2- 5%, NO 3 - 20%;
[0020] Take 100 g of the above-mentioned nitrogen-containing and sulfur-containing iron salt, and denitrify at 550° C. for 1.0 h to obtain flue gas containing nitrogen oxides and 73 g of sulfur-containing iron salt. Flue gas containing nitrogen oxides is recovered for the production of nitric acid; the composition (mass percentage) of sulfur-containing iron salt is: Fe 56%, SO 4 2- 6.8%, NO 3 - 4 2- 0.18%, NO 3 - 0.03%, yield 90.24%; the solution composition after ammonia leaching is SO 4 2- 13.06 g / L, NO 3 - 4 + 6.12g / L. The ammonia immersion solution is evaporated and crystallized to obtain ammonium sulfate crystals and condensed water. The contents of impurity elements Fe and Ni in ammonium sulfate crystals are less than 0.001%, which are exported directly and condensed water is recycled. The removal...
Embodiment 3
[0022] The composition (mass percentage) of nitrogen-containing and sulfur-containing iron salt in this embodiment is: Fe 40%, SO 4 2- 35%, NO 3 - 10%;
[0023] Take 100 g of the above-mentioned nitrogen-containing and sulfur-containing iron salt, and denitrify at 500° C. for 45 minutes to obtain flue gas containing nitrogen oxides and 86 g of sulfur-containing iron salt. Flue gas containing nitrogen oxides is recovered for the production of nitric acid; the sulfur-containing iron salt composition (mass percentage) is: Fe 45%, SO 4 2- 38%, NO 3 - 4 2- 0.23%, NO 3 - 0.03%, yield 74.71%; the solution composition after ammonia leaching is SO 4 2- 75.55 g / L, NO 3 - 4 + 34.20g / L. The ammonia immersion solution is evaporated and crystallized to obtain ammonium sulfate crystals and condensed water. The contents of impurity elements Fe and Ni in ammonium sulfate crystals are less than 0.001%, which are exported directly and condensed water is recycled. The rem...
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