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Electrochemical Fluorination of Room Temperature Molten Salt

 

Akimasa TASAKA, Yoshio SHODAI,

Junpei YAMASHITA, Taro

KINUMOTO, Akihiro MIYASAKA ,

and Kunitaka MOMOTA*

 

Department of Molecular Science and

Technology, Doshisha University

Miyako-dani 1-3, Tadara, Kyotanabe,

Kyoto 610-0321, Japan

* Morita Chemicals Industries Co. Ltd.,

Higashi-mikuni 3-12, Yodogawa-ku,

Osaka 532-0002, Japan

 

Perfluorotrimethylamine, (CF3)3N, is expected to be a new gas for dry etching of a semiconductor and a cleaning gas for CVD chamber used in semiconductor and electronics industries, being able to be obtained by electrolysis of trimethylamine, (CH3)3N, dissolved in anhydrous HF with the Ni anode [1]. The melt of (CH3)4NFmHF with and without alkali metal fluoride is used as the electrolyte at room temperature in order to develop a new process for electrolytic produc-

tion of (CF3)3N.

This paper deals with the formation ratio of (CF3)3N to the overall anode gas and the anode consumption during electrolysis of the melts of (CH3)4NFmHF with and without alkali metal fluoride such as LiF, KF and CsF using the Ni based composite and the LiNiO2 coating Ni sheet anodes as well as the Ni sheet anode.


The electrolytic cell and the experimental procedure were described in the previous paper [2]. The electrolytes were prepared with addition of LiF into the (CH3)4NFmHF melt or mixing the (CH3)4NFmHF melt with KF2HF or CsF2HF. The reference electrode was Ag/AgClO4 in CH3CN containing (C2H5)4NBF4 as the supporting electrolyte.  The anode gas collected through the NaF pellet tube was fractionated by means of gas chromatography (column packing: Porapack R, carrier gas: He) and the constituents having the respective peaks on the chromatogram were identified by mass spectroscopy.

Electrolysis of the (CH3)4NFmHF melts (m = 4 and 5) with and without CsF2HF was conducted with the Ni anode polarized at 6.0 V for 100 hours. The ratio of each constituent to the overall anode gas obtained in electrolysis and the average current densities are summarized in Table 1. The anode gas was composed of CF4, NF3, C2F6, CHF3 and (CF3)3N. Although no (CF3)3N was detected in the anode gas formed in electrolysis of the (CH3)4NF4HF melt only, the amount of electricity may be too small to form it. The ratio of (CF3)3N to the overall anode gas in the mixed melt of (CH3)4NF4HF + 30wt% CsF2HF was 0.42 and its value was the largest in our experiments. Also, the current density increased with increasing the content of CsF2HF in the mixed melt.

Electrolysis of the (CH3)4NF5HF melt was also conducted with the Ni based composite anodes polarized at 5.0 V for 100 hours. The composition of the anode gas was similar to that obtained with the Ni sheet anode. The average current density on the Ni-NiO composite anode in this melt was 30.0 mAcm-2 and it was large compared with that observed in the mixed melt of (CH3)4NF4HF + 30wt% CsF2HF. The results obtained in electrolysis of the mixed melt of (CH3)4NFmHF with LiF and KF2HF using the Ni sheet, the Ni based composite, the LiNiO2 coating Ni sheet, and the carbon anodes will be also discussed.

References

[1]  J.H. Simons, US Patent 2, 616, 927 (1952).

[2]  K. Momota, K.Kato, M.Morita, Y. Matuda, Electrochimica Acta, 39, 681

    (1994).

Table 1 The constituents of the anode gas and the average current densities for electrolysis of (CH3)4NF?mHF melt with and without CsF?2HF for 100 hours with the anode polarized at 6.0V