Method for combined utilization of iron-based pigment wastewater and reduced titanium tail gas
A technology for iron-based pigments and wastewater, which is applied in the field of iron-based pigment wastewater preparation, can solve problems such as loss of chemical value, non-utilization, and environmental pollution, and achieve the goals of reducing the risk of precipitation and scaling, creating economic value, and reducing production costs Effect
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Embodiment 1
[0043] 1. According to the patent publication number, it is CN 108557877A step to generate iron-based pigments, and the content of sodium sulfate in the iron-based pigment mother liquor is 9.8%, and the solid-liquid separation is carried out by ceramic membrane (cut-off particle diameter 100nm); the sodium sulfate content in the iron-based pigment washing water is 1.2%, first separated by ceramic membrane, and then concentrated by reverse osmosis membrane, the content of sodium sulfate on the concentrated water side is 10.3%, and the reverse osmosis concentrated liquid is mixed with the ceramic membrane clear liquid;
[0044] 2. After the reverse osmosis concentrated liquid is mixed with the ceramic membrane liquid, react with carbide slag, wherein the carbide slag and water are beaten, and the ratio is calcium carbide slag: water = 1:3, g / mL, and the reaction end point is 9.6;
[0045] 3. After the reaction of calcium carbide slag, the system is filtered through a filter press...
Embodiment 2
[0049] 1. According to the patent publication number, it is CN 108557877A step to generate iron-based pigments, and the content of sodium sulfate in the iron-based pigment mother liquor is 8.5%, and solid-liquid separation is carried out by ceramic membrane (cut-off particle diameter 100nm); the sodium sulfate content in the iron-based pigment washing water is 0.8%, first separated by ceramic membrane, and then concentrated by reverse osmosis membrane, the content of sodium sulfate on the concentrated water side is 11.2%, and the reverse osmosis concentrated liquid is mixed with the ceramic membrane clear liquid;
[0050] 2. After the reverse osmosis concentrated liquid is mixed with the ceramic membrane clear liquid, it reacts with calcium carbide slag, wherein the carbide slag and water are beaten, and the ratio is calcium carbide slag: water = 1:3, and the reaction end point is 9.8;
[0051] 3. After the reaction of calcium carbide slag, the system is filtered through a filt...
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