Method for isolating and producing enriched 28Si, 29Si and 30Si by serially connected multiple towers and apparatus used by method
An enrichment and obtained technology, applied in separation methods, chemical instruments and methods, dispersed particle separation, etc., to achieve the effect of improving separation efficiency, reducing difficulty, and reducing height
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Embodiment 1
[0046] In this embodiment, both the first chemical exchange system and the second chemical exchange system use ethanol as complexing agent, SiF 4 A separation system is formed between the gas and the silicon tetrafluoride ethanol complex.
[0047] The specific process is as follows.
[0048] In the first chemical exchange system, SiF 4 The gas enters from the bottom of the first complexing tower 1, and reacts with the ethanol sprayed down from the top of the tower at 0-10°C and 0.1-0.2Mpa (absolute pressure) to form a silicon tetrafluoride ethanol complex, which is formed by the second The process at the bottom of a complexing tower 1 enters the buffer tank 15; then the SiF that is sprayed down and flows from bottom to top is pumped to the top of the first chemical exchange tower assembly 2 by a pump 16 4 The gas undergoes a chemical exchange reaction at 5~10°C and 0.1~0.2Mpa (absolute pressure); the silicon tetrafluoride ethanol complex flowing out of the first chemical exc...
Embodiment 2
[0051] In this embodiment, the first chemical exchange system uses methanol as a complexing agent, and the second chemical exchange system uses n-propanol as a complexing agent. In the two systems, SiF 4 Separate systems are formed between the gas and the silicon tetrafluoride methanol complex and the silicon tetrafluoride n-propanol complex.
[0052] The specific process is as follows.
[0053] In the first chemical exchange system, SiF 4 The gas enters from the bottom of the first complexing tower 1, and reacts with the methanol sprayed down from the top of the tower at 5~15°C and 0.1~0.2Mpa (absolute pressure) to form a silicon tetrafluoride ethanol complex. The process at the bottom of a complexing tower 1 enters the buffer tank; then the pump 16 hits the top of the first chemical exchange tower assembly 2, which is sprayed down and flows from bottom to top. 4 The gas undergoes a chemical exchange reaction at 10~15°C and 0.1~0.2Mpa (absolute pressure); the silicon tetraf...
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