A device and application for preparing nitrogen trifluoride gas
A technology of nitrogen trifluoride and gas, which is applied in the field of preparing nitrogen trifluoride gas, can solve problems such as the reduction of electrolysis efficiency and affect the health of employees, achieve continuous electrolysis, reduce manual high-temperature and toxic operations, and realize the effect of automation
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0069] A kind of preparation NF in this embodiment 3 The reaction kettle 15, the storage tank 16 and the electrolyzer 20 of the device of the gas are the same as the comparative example 2.
[0070] The application steps of the device are as follows:
[0071] (1) Electrolyte synthesis and storage
[0072] When NH 3 NH was detected by tank flow meter 7 and HF tank flow meter 8 respectively 3 and HF cumulative flow reaches 4.7×10 5 L and 1.16×10 6 During L, send signal to automatic control system 11; All the other are with comparative example 3 steps (1).
[0073] (2)NF 3 Electrolysis and replenishment
[0074] With comparative example 2 step (2).
[0075] The electrolysis temperature of the electrolytic cell 20 is 120° C. during the operation period. The electrolysis process of the electrolytic cell 20 is as follows: 1) The electrolysis time is up to 5h under the condition of a voltage of 5.5V, and the gas generated by the anode is measured, NF 3 The volume percentage ...
Embodiment 2
[0077] A kind of preparation NF in this embodiment 3 The reaction kettle 15, the storage tank 16 and the electrolyzer 20 of the device of the gas are the same as the comparative example 2.
[0078] The application steps of the device are as follows:
[0079] (1) Electrolyte synthesis and storage
[0080] NH 3 Storage tank flowmeter 7 and HF storage tank flowmeter 8 respectively adjust NH 3 and HF flow to 220L / min and 585L / min; when NH 3 NH was detected by tank flow meter 7 and HF tank flow meter 8 respectively 3 and HF cumulative flow reaches 4.49×10 5 L and 1.19×10 6 During L, send signal to automation control system 11; In reactor 15, NH 3 Gas reacts with HF gas to form NH 4 F.1.9HF electrolyte; the rest are the same as step (1) of comparative example 3.
[0081] (2)NF 3 Electrolysis and replenishment
[0082] With comparative example 2 step (2).
[0083] The electrolysis temperature of the electrolytic cell 20 is 120° C. during the operation cycle. The electrol...
Embodiment 3
[0085] A kind of preparation NF in this embodiment 3 The reaction kettle 15 of the gas device is the same as Comparative Example 2; the storage tank 16 is a 4000L nickel container, the highest liquid level is 700mm, and the lowest is 100mm; The electrolyte liquid level of tank 20 is the highest 650mm, the lowest is 530mm, and the anode and cathode are nickel plates.
[0086] The application steps of the device are as follows:
[0087] (1) Electrolyte synthesis and storage
[0088] When NH 3 NH was detected by tank flow meter 7 and HF tank flow meter 8 respectively3 and HF cumulative flow reaches 4.7×10 5 L and 1.16×10 5 During L, send signal to automatic control system 11; All the other are with comparative example 3 steps (1).
[0089] (2)NF 3 Electrolysis and replenishment
[0090] When the electrolytic tank level gauge 21 shows a value of 650mm, a signal is sent to the automatic control system 11;
[0091] Electrolytic production of NF 3 During the gasification pro...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
