Decomposition and filtration method during alumina production process
A filtration method and production process technology, applied in the direction of alumina/hydroxide, etc., can solve problems such as increased operating costs, cumbersome process transfers, increased investment, etc., to reduce investment costs and personnel operations, save intermediate links, The effect of saving land
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0024] The structure of the decomposition and filtration system in the alumina production process is as follows: figure 1 As shown, the decomposition tank system is composed of 12 decomposition tanks connected in series including the first decomposition tank 1, the second decomposition tank 2, the penultimate decomposition tank 3 and the final decomposition tank 4; the vertical disc filter 5, the vacuum liquid receiving tank 6 And the gas-liquid separator 7 is arranged above the first decomposition tank 1;
[0025] The two distribution heads of the vertical disc filter 5 communicate with the vacuum liquid receiving tank 6, the air outlet at the top of the vacuum liquid receiving tank 6 communicates with the gas-liquid separator 7, and the air suction port above the gas-liquid separator 7 communicates with the vacuum pump 12;
[0026] A liquid outlet is provided below the vacuum liquid receiving tank 6 and the gas-liquid separator 7, and a mother liquor buffer tank 8 is provide...
Embodiment 2
[0041] The structure of the decomposition and filtration system in the alumina production process is different from that of Embodiment 1 in that the decomposition tank system is composed of 14 decomposition tanks connected in series;
[0042] The working method differs from Example 1 in that: the temperature of the slurry decomposed in the penultimate decomposition tank is 48-50°C, its solid content is 780g / L, the content of alumina is 105g / L, and the content of sodium hydroxide is 182g / L;
[0043] The content of aluminum oxide in cold semen is 190g / L, and the content of sodium hydroxide is 165g / L;
[0044] The water content of the filter cake filtered by the vertical disc filter is 25%, and the solid content after mixing with cold semen is about 780g / L;
[0045] The decomposition time of the filter cake diluted with cold semen in the decomposition tank system is 50h;
[0046] The solids content of the underflow of the classifying cyclone was 800 g / L.
Embodiment 3
[0048] The structure of the decomposition and filtration system in the alumina production process is the same as in Embodiment 1, the difference being that the decomposition tank system is composed of 16 decomposition tanks connected in series;
[0049] The working method is the same as in Example 1, the temperature of the slurry decomposed in the penultimate decomposition tank is 48~50°C, its solid content is 820g / L, the content of alumina is 100g / L, and the content of sodium hydroxide is 178g / L ;
[0050] The content of aluminum oxide in cold semen is 195g / L, and the content of sodium hydroxide is 170g / L;
[0051] The water content of the filter cake filtered by the vertical disc filter is 30%, and the solid content after mixing with cold semen is about 820g / L;
[0052]The decomposition time of the filter cake diluted with cold semen in the decomposition tank system is 52 hours;
[0053] The solids content of the underflow of the classifying cyclone was 900 g / L.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 