A kind of production equipment and method of high-purity gallium
A production method and high-purity technology, applied in the field of high-purity gallium production equipment, can solve the problems of insufficient heat exchange between the medium and gallium liquid, the inability to effectively control the crystallization solidification rate, and difficulty in forming and agglomerating impurities, achieving good application prospects , Improve heat exchange efficiency and shorten production cycle
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Embodiment 1
[0025] A high-purity gallium production equipment, such as figure 1 As shown, it includes a crystallization tank 1, a medium circulation tank, a thermal insulation layer 7 and a liquid gallium discharge device; the upper left side of the crystallization tank 1 is provided with a crystallization tank inlet 3, and the upper right side is provided with a crystallization tank outlet 4; the medium circulation tank It includes n independent medium circulation tanks, where n is an integer, 5≤n≤10; each medium circulation tank is composed of a circulation body, a medium inlet and a medium outlet, and the n medium circulation tanks are sequentially arranged from left to right Distributed laterally along the crystallization tank 1, the circulation body of each medium circulation tank is located inside the crystallization tank 1, and the medium inlet and medium outlet extend through the crystallization tank 1 to the outside of the crystallization tank 1; the heat insulation layer 7 is dis...
Embodiment 2
[0034] Such as figure 2 As shown, the difference between the device of this embodiment and Embodiment 1 lies in: (1) n is 7.
[0035] Compared with Example 1, the production steps of this embodiment differ in that: (1) both the cold medium and the heat medium are ethylene glycol; (2) the flow rate of the cold medium is 10 L / h, and the medium temperature is 2°C; (3) The heat medium flow rate of the first medium circulation tank 201-the sixth medium circulation tank 206 is 10L / h, and the medium temperature is 35°C; (4) The heat medium flow rate of the seventh medium circulation tank 207 is 10L / h, and the medium temperature (5) Step 6, repeat steps 2 to 5 5 times, so that the gallium in the crystallization tank 1 is crystallized again 5 times.
[0036] Table 3 is the impurity content table of the high-purity gallium prepared in this embodiment. The impurity elements above the detection limit in the high-purity gallium prepared by the method of the present invention include Cu ...
Embodiment 3
[0041] Such as Figure 3-Figure 4 As shown, the difference between the device of this embodiment and Embodiment 1 is: (1) n is 5; (2) the shape of the crystallization tank 1 is a cuboid, and (3) the circulation main body of each medium circulation tank is in a row shape.
[0042] Compared with Example 1, the production steps of this embodiment differ in that: (1) both the cold medium and the heat medium are ethylene glycol; (2) the flow rate of the cold medium is 10L / h, and the medium temperature is 25°C; (3) The heat medium flow rate of the first medium circulation tank 201-the fourth medium circulation tank 204 is 10L / h, and the medium temperature is 80°C; (4) The heat medium flow rate of the fifth medium circulation tank 205 is 10L / h, and the medium temperature 80°C; (5) Step 6, repeat steps 2 to 5 6 times, so that the gallium in the crystallization tank 1 is crystallized again 6 times; (6) The protective gas is high-purity argon.
[0043] Table 4 is the impurity content t...
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