Boric sludge comprehensive utilization method for preparing nanometer magnesia and nanocrystalline iron oxide
A nano-iron oxide and nano-magnesium oxide technology, applied in the nano field, can solve the problems of complex process, non-conformity and high energy consumption, and achieve the effects of increasing added value, reducing exhaust emissions and saving energy.
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Embodiment 1
[0030] The XRD of boron mud used is attached figure 1 As shown, it is mainly composed of magnesium carbonate, magnesium silicate, iron silicate, iron oxide and other phases, and its chemical composition is shown in Table 1.
[0031] Table 1 Chemical composition of boron mud / mass%
[0032] composition B 2 o 3 MgO CaO SiO 2 Fe 2 o 3 Al 2 o 3 content 2.5 35 5 18 25 2
[0033] (1) Carry out low-temperature pressure leaching of boron mud in hydrochloric acid system, and then filter and separate to obtain magnesium chloride, ferric chloride leachate and borosilicate-rich slag. The low-temperature pressure leaching conditions are: the solid-to-liquid ratio of boron mud to hydrochloric acid is 1kg: 5L, the leaching temperature is 120°C, the concentration of hydrochloric acid is 8mol / L, the leaching time is 30min, and the leaching rates of magnesium and iron are 95.5% and 95.2% respectively;
[0034] (2) Add MgO or Fe to the magnesium ...
Embodiment 2
[0039] Boron mud used is with embodiment 1.
[0040] (1) Carry out low-temperature pressure leaching of boron mud in hydrochloric acid system, and then filter and separate to obtain magnesium chloride, ferric chloride leachate and borosilicate-rich slag. The low-temperature pressure leaching conditions are: the solid-to-liquid ratio of boron mud to hydrochloric acid is 1kg: 10L, the leaching temperature is 100℃, the concentration of hydrochloric acid is 5mol / L, the leaching time is 90min, and the leaching rates of magnesium and iron are 96.5% and 95.5% respectively;
[0041] (2) Add MgO or Fe to the magnesium chloride and ferric chloride leaching solution obtained in step (1) 2 o 3 Adjust the pH value of the leaching solution to 3.2. In order to effectively precipitate and separate iron, add H during the precipitation process. 2 o 2 Oxidize the ferrous ions in the leach solution to ferric ions, precipitate the iron ions in the form of ferric hydroxide, and then filter and s...
Embodiment 3
[0046] Boron mud used is with embodiment 1.
[0047] (1) Carry out low-temperature pressure leaching of boron mud in hydrochloric acid system, and then filter and separate to obtain magnesium chloride, ferric chloride leachate and borosilicate-rich slag. The low-temperature pressure leaching conditions are: the solid-to-liquid ratio of boron mud to hydrochloric acid is 1kg: 15L, the leaching temperature is 80°C, the concentration of hydrochloric acid is 3mol / L, the leaching time is 60min, and the leaching rates of magnesium and iron are 97.5% and 96.2% respectively;
[0048] (2) Add MgO or Fe to the magnesium chloride and ferric chloride leaching solution obtained in step (1) 2 o 3 Adjust the pH value of the leaching solution to 3.5. In order to effectively precipitate and separate iron, add H during the precipitation process. 2 o 2 Oxidize the ferrous ions in the leach solution to ferric ions, precipitate the iron ions in the form of ferric hydroxide, and then filter and s...
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