Method for preparing barium-based glass frit with barium slag
A technology of glass frit and glass melt, which is applied in the fields of chemical instruments and methods, inorganic chemistry, water/sludge/sewage treatment, etc., can solve the problems such as high aluminum can not be used, achieve less air bubbles, realize circular economy, protect The effect of ecological environment
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Embodiment 1
[0061] (1) Use a ball mill to grind the barium slag to 100 mesh, and adjust the barium slag slurry with water, wherein the mass ratio of solid to liquid in the slurry is 1:2.5.
[0062] (2) The slurry pump feeds the barium slag slurry into the leaching pipeline, and at the same time, the sulfuric acid pump pumps 105% sulfuric acid into the pipeline, with an initial pressure of 16kg / cm 2 , terminal pressure 0.5kg / cm 2 , the pH value of the reaction liquid is controlled to be 1, and the reaction time is 5 minutes. After the reaction, the material enters the gas-liquid separation buffer tank for gas-liquid separation.
[0063] (3) The separated gas enters the absorption tower and is absorbed by sodium hydroxide to prepare sodium sulfide. The mud enters the settling tank, and the overflow liquid from the upper part of the settling tank is filtered and purified, and then enters the hydrolysis reaction tank to prepare polyferric aluminum sulfate water purifying agent.
[0064] (4...
Embodiment 2
[0067] (1) Use a ball mill to grind the barium slag to 200 mesh, and adjust the barium slag slurry with water, wherein the mass ratio of solid to liquid in the slurry is 1:1.25.
[0068] (2) The slurry pump feeds the barium slag slurry into the leaching pipeline, and at the same time, the sulfuric acid pump pumps 98% sulfuric acid into the pipeline, with an initial pressure of 10kg / cm 2 , terminal pressure 8kg / cm 2 , the pH value of the reaction liquid is controlled to be 2, and the reaction time is 10 minutes. After the reaction, the material enters the gas-liquid separation buffer tank for gas-liquid separation.
[0069] (3) The separated gas enters the absorption tower and is absorbed by sodium hydroxide to prepare sodium sulfide. The mud enters the settling tank, and the overflow liquid from the upper part of the settling tank is filtered and purified, and then enters the hydrolysis reaction tank to prepare polyferric aluminum sulfate water purifying agent.
[0070] (4)...
Embodiment 3
[0073] (1) Use a ball mill to grind the barium slag to 300 mesh, and adjust the barium slag slurry with water, wherein the mass ratio of solid to liquid in the slurry is 1:1.25.
[0074] (2) The slurry pump feeds the barium slag slurry into the leaching pipeline, and at the same time, the sulfuric acid pump pumps 93% sulfuric acid into the pipeline with an initial pressure of 10kg / cm 2 , terminal pressure 2kg / cm 2 , the pH value of the reaction liquid was controlled to be 3, and the reaction time was 20 minutes. After the reaction, the material enters the gas-liquid separation buffer tank for gas-liquid separation.
[0075] (3) The separated gas enters the absorption tower and is absorbed by sodium hydroxide to prepare sodium sulfide. The mud enters the settling tank, and the overflow liquid from the upper part of the settling tank is filtered and purified, and then enters the hydrolysis reaction tank to prepare polyferric aluminum sulfate water purifying agent.
[0076] (4...
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