Method for preparing sintered glass-ceramic through melting-free process
A glass-ceramic and process technology, which is applied in the field of preparing sintered glass-ceramic with iron phosphate, can solve the problems of high temperature melting and energy consumption of main and auxiliary materials, achieve good energy saving effect, good environmental benefit, and solve the problem of solid waste and waste liquid disposal. Effect
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Embodiment 1
[0020] Lithium iron phosphate is acid leached and filtered to obtain acid leaching solution and acid leaching residue. During the acid leaching process, the mass ratio of water to lithium iron phosphate powder is 2:1, the amount of nitric acid added is 3mol / L, and 30% The amount of hydrogen peroxide is 3ml: 1g lithium iron phosphate powder, the leaching temperature is 30°C, and the leaching time is 12 hours; the acid leaching solution obtained by acid leaching is subjected to lithium precipitation and filtration to obtain lithium slag and lithium precipitation solution, and the lithium slag is returned to lithium recovery , during the process of lithium precipitation and filtration, add sodium bicarbonate as lithium precipitation agent, add sodium bicarbonate until the solution does not produce precipitation, the temperature of lithium precipitation is 70 ° C, and the stirring time of lithium precipitation is 0.5 hours; the acid leaching residue obtained by acid leaching and th...
Embodiment 2
[0022] Lithium iron phosphate is subjected to acid leaching and filtration to obtain acid leaching solution and acid leaching residue. During the acid leaching process, the mass ratio of water to lithium iron phosphate powder is 3:1, the amount of nitric acid added is 5mol / L, and 30% The amount of hydrogen peroxide is 5ml: 1g lithium iron phosphate powder, the leaching temperature is 60°C, and the leaching time is 36 hours; the acid leaching solution obtained by acid leaching is subjected to lithium precipitation and filtration to obtain lithium slag and lithium precipitation solution, and the lithium slag is returned to lithium recovery , during the process of lithium precipitation and filtration, add sodium bicarbonate as lithium precipitation agent, add sodium bicarbonate until the solution does not produce precipitation, the temperature of lithium precipitation is 90 ° C, and the stirring time of lithium precipitation is 2 hours; the acid leaching residue obtained by acid le...
Embodiment 3
[0024] Lithium iron phosphate is acid leached and filtered to obtain acid leaching solution and acid leaching residue. During the acid leaching process, the mass ratio of water to lithium iron phosphate powder is 2.5:1, the amount of nitric acid added is 4mol / L, and 30% The amount of hydrogen peroxide is 4ml: 1g lithium iron phosphate powder, the leaching temperature is 40°C, and the leaching time is 24 hours; the acid leaching solution obtained by acid leaching is subjected to lithium precipitation and filtration to obtain lithium slag and lithium precipitation solution, and the lithium slag is returned to lithium recovery , during the lithium sinking filtration process, add sodium bicarbonate as a lithium sinking agent, add sodium bicarbonate until the solution does not produce precipitation, the lithium sinking temperature is 80 ° C, and the lithium sinking stirring time is 1 hour; the acid leaching residue obtained by acid leaching and the heavy lithium solution obtained by...
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