Method for recovering and utilizing sewage generated during technology process of acid method for extracting aluminum oxide from fly ash
A technology of sewage recycling and alumina, applied in chemical instruments and methods, aluminum sulfate, water/sewage treatment, etc., can solve the problem of undisclosed alumina extraction technology, such as sewage recycling and utilization methods.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
example 1
[0019] (1) Raw material preparation: the concentration of aluminum ions in the waste water of the fly ash acid method for extracting alumina technology is 0.13mol / L, and the concentration of sulfuric acid is 6.7%;
[0020] (2) Get above-mentioned sewage 100mL, scrap steel slag 5g, scrap steel slag is added in the sewage, stir evenly, join in the reactor;
[0021] (3) Reaction at a reaction temperature of 60° C. for 1 h;
[0022] (4) Filter the reacted solution, combine impurity removal and crystallization to obtain aluminum sulfate and ferric sulfate solutions; the separation and conversion of aluminum sulfate and ferric sulfate into corresponding oxides are known technologies, and will not be repeated here.
[0023] Under this condition, the concentration of sulfuric acid in the sewage drops below 0.5%, the recovery rate of aluminum reaches 85.0%, and the recovery rate of iron reaches 82.9%.
example 2
[0025] (1) Raw material preparation: the concentration of aluminum ions in the waste water of the fly ash acid method for extracting alumina technology is 0.21mol / L, and the concentration of sulfuric acid is 11.4%;
[0026] (2) Get above-mentioned sewage 100mL, scrap steel slag 10g, scrap steel slag is added in the sewage, stir evenly, join in the reactor;
[0027] (3) reacting at a reaction temperature of 70° C. for 1.5 h;
[0028] (4) Filter the reacted solution, combine impurity removal and crystallization to obtain aluminum sulfate and ferric sulfate solutions; the separation and conversion of aluminum sulfate and ferric sulfate into corresponding oxides are known technologies, and will not be repeated here.
[0029] Under this condition, the sulfuric acid concentration in the sewage drops below 0.5%, the recovery rate of aluminum reaches 86.3%, and the recovery rate of iron reaches 84.1%.
example 3
[0031] (1) Raw material preparation: the concentration of aluminum ions in the waste water of the fly ash acid method for extracting alumina technology is 0.27mol / L, and the concentration of sulfuric acid is 16.3%;
[0032] (2) Get above-mentioned sewage 100mL, scrap steel slag 15g, scrap steel slag is added in the sewage, stir evenly, join in the reactor;
[0033] (3) reacting at a reaction temperature of 90° C. for 2.5 hours;
[0034] (4) Filter the reacted solution, combine impurity removal and crystallization to obtain aluminum sulfate and ferric sulfate solutions; the separation and conversion of aluminum sulfate and ferric sulfate into corresponding oxides are known technologies, and will not be repeated here.
[0035] Under this condition, the concentration of sulfuric acid in the sewage drops below 0.5%, the recovery rate of aluminum reaches 90.4%, and the recovery rate of iron reaches 87.3%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More