Patent Application
20100121117
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1. Field of the Invention
The present invention relates to a process of preparing decafluorocyclohexene by allowing hexafluorobenzene to react with a fluorinating agent, which yields decafluorocyclohexene with high selectivity, and to a fluorinating agent which is used in the process.
More specifically, the present invention relates to a process of preparing decafluorocyclohexene (C6F10) by allowing hexafluorobenzene (C6F6) to react with a fluorinating agent. The invention also relates to a fluorinating agent comprising 1-50 wt % of cobalt fluoride (CoF2) and 50-99 wt % of other metal fluoride selected one at least among calcium fluoride (CaF2), magnesium fluoride (MgF2), aluminum fluoride (AlF3) sodium fluoride (NaF) and potassium fluoride (KF).
2. Description of Related Art Including Information Disclosed Under 37 CFR 1.97 and 37 CFR 1.98
Decafluorocyclohexene (C6F10) is a compound having a molecular weight of 262 and a boiling point of 51-53° C. It's chemical species present in the plasma state is similar to octafluorocyclopentene (C5F8), an etching gas which is used for polysilicon or silicon oxide in the prior art.
The present inventors have considered that decafluorocyclohexene (C6F10) which can be commercially prepared through an easy and simple process could be a useful etching gas, and have developed a preparation process thereof.
GB Patent No. 920,796 discloses a process of preparing decafluorocyclohexene (C6F10) by heating undecafluorocyclohexane (C6F11H) at 700-900° C.
In this process, the reaction temperature has maintained at 700° C. at lowest, but the yield was as low as 61-85%. In GB Patent No. 1,017,814, decafluorocyclohexene (C6F10) was prepared with low yield bypassing undecafluorocyclohexane (C6F11H) through sodium fluoride pellets at a reaction temperature of 320° C. In addition, the preparation of undecafluorocyclohexane (C6F11H) as the raw material is carried out in a complicated manner, thus, the industrial application thereof is greatly limited.
U.S. Pat. No. 3,331,880 discloses a process of preparing decafluorocyclohexene (C6F10) by allowing an excess amount of antimony pentafluoride (SbF5) to react with chloroperfluorocyclohexene at a temperature of 120° C. When heptafluorotrichlorocyclohexene is used as the raw material, the yield of decafluorocyclohexene (C6F10) is as extremely low as 7.1%.
In addition, a process is known for preparing decafluorocyclohexene (C6F10) by allowing undecafluorocyclohexane (C6F11H) to react with KOH (Fluorocarbon and their derivatives. R. E. bank, 1970).
It is an object of the present invention to provide a process of preparing high-purity decafluorocyclohexene in high yield by fluorinating hexafluorobenzene (C6F6) as a starting material and to provide a fluorinating agent which is used in the fluorination process.
The fluorinating agent developed in the present invention is a powder and is prepared by mechanically mixing 1-50 wt % of cobalt difluoride (CoF2) with 50-99 wt % of other metal fluoride selected one at least among calcium fluoride (CaF2), magnesium fluoride (MgF2), aluminum(III) fluoride (AlF3), sodium fluoride (NaF) and potassium fluoride (KF) and bringing the mixture into contact with fluorine gas, thus preparing an activated fluorinating agent. Reactivity and selectivity are vary depending on the ratio of metal fluoride added, and this fluorinating agent is suitable for selectively synthesizing decafluorocyclohexene (C6F10).
The activation for the fluorinating agent is carried out by allowing CoF2 and the metal fluoride to react with fluorine gas so as to activate the metal fluoride, and it proceeds according to the following reaction equation:
CoF2+½F2→CoF3
Metal fluorides other than CoF2 no longer undergo a fluorination reaction during the process of activating the fluorinating agent.
CoF3 is a good fluorinating agent but unstable compound which is reduced into CoF2 immediately upon contact with air and is very difficult to store.
When C6F6 is used as a starting material to prepare C6F10, with CoF3 as a fluorinating agent, the reaction product will be obtained as a mixture of C6F8, C6F10 and C6F12 in various ratios. Particularly if only CoF3 is used, most of the reaction product will be C6F12.
Herein, the reaction of C6F6 is influenced by the fluorinating ability of the fluorinating agent and the reaction temperature, and the mixing ratio of components of the metal oxides.
Accordingly, in order to increase the selectivity of the target compound (C6F10), it is required to maintain reaction condition suitable therefor.
The present inventors have conducted various experiments to determine reaction condition in which the selectivity of the target compound (C6F10) can be maximized. As a result, the present inventors have found that the fluorination rate of C6F6 can be adjusted by adjusting the weight ratio of CoF3 in the fluorinating agent, and have found reaction conditions, in which the selectivity of C6F10 is exceptionally high, by selecting and employing a metal fluoride as a diluting agent to adjust the content ratio of CoF3 without adversely affecting a fluorination reaction, thereby completing the present invention.
Herein, the metal fluoride is preferably CaF2, MgF2, AlF3, NaF or KF.
In order to inhibit C6F6 from proceeding to C6F12 due to the high activity of CoF3 and to control reaction conditions, the activity of CoF3 needs to be adjusted to a low level.
The process of preparing decafluorocyclohexene using the activated fluorinating agent is characterized in that, as a method of adjusting the reactivity of the fluorinating agent in order to obtain the optimal yield, in addition to adjusting the ratio of metal fluoride added, any one of nitrogen (N2), helium (He) and argon (Ar) that are inert gases is supplied together with the reactant.
When inert gas is introduced into the fluorination reaction of C6F6, the contact time between the raw material gas (C6F6) and the fluorinating agent can be reduced. Thus, the fluorination reaction can be controlled through the introduction of inert gas.
The fluorinating agent comprises CoF2 as an active ingredient and metal fluoride as a diluen, and the content of the metal fluoride is preferably 50-99 wt % based on 100 wt % of the fluorinating agent.
Under the conditions of a fluorination reaction that uses the fluorinating agent of the present invention, the content of metal fluoride, the reaction temperature and the amount of inert gas supplied influence the fluorination reaction. If the content of metal fluoride is more than 99%, the fluorination rate will be excessively low, and if it is less than 50 wt %, the control of the reaction will be difficult.
The content of metal fluoride is preferable for 50-90 wt % to control the reaction rate at the reaction temperature of 60˜200° C.
In the preparation process of the present invention, hexafluorobenzene is used as a starting material. Hexafluorobenzene (C6F6) is a compound which contains a fluorine atom bonded to each of six unsaturated carbons, has no hydrogen, and is liquid at room temperature. The use of benzene, chlorobenzene or a hydrocarbon as a starting material is not suitable not only because Hydrogen fluoride(HF) is produced, which needs additional process of removing acid, but also because many side products including isomers are produced, thus making a purification process very complicated.
In the present invention, a mixture of cobalt difluoride (CoF2) and metal fluoride is charged into a reactor and activated with fluorine gas at 200-400° C., thus preparing an activated fluorinating agent. C6F6 together with inert gas is supplied and allowed to react with the activated fluorinating agent at a reaction temperature of 60-200° C., thus preparing C6F10. After completion of the reaction, the fluorinating agent is activated again with fluorine gas and stands by for the next reaction. For commercial application, the reaction must be continuously carried out, and thus two reactors are used such that the process of activating the fluorinating agent and the reaction process are repeatedly carried out.
Hereinafter, the preparation process of the present invention will be described with reference to the preparation system shown in
The above and other objects, features and advantages of the present invention will be more clearly understood from the following detailed description taken in conjunction with the accompanying drawing.
In a horizontal-type or vertical-type reactor, a fluorinating agent obtained by mechanically mixing 1-50 wt % of powdery cobalt difluoride (CoF2) with 50-99 wt % of at least one of powdery calcium fluoride (CaF2), magnesium fluoride (MgF2) aluminum fluoride (AlF3), sodium fluoride (NaF) and potassium fluoride (KF) is uniformly charged in an amount corresponding to about 70% of the volume of the reactor and activated with fluorine gas at a temperature of 200-400° C. After completion of the activation, the remaining fluorine gas is removed while supplying inert gas into the reactor. When the introduced fluorine gas is no longer consumed in the reactor the activation of CoF2 is ended.
Process for Synthesizing C6F10
After the activation of the fluorinating agent is completed, the temperature of the reactor is lowered to 60-200° C., and the raw material C6F6 is quantitatively passed through a preheater, and then sent to the reactor. The reaction product from the reactor is condensed in a trap at a temperature ranging from −10° C. to 0° C. to capture unreacted reactant and products having higher boiling points, and the remaining product is condensed in a second trap of acetone/liquid nitrogen slush at a temperature ranging from −60° C. to −80° C.
Hereinafter, the present invention will be described in further detail with reference to examples.
As shown in
Then, the raw material C6F6 was quantitatively passed through a preheater 7 at a temperature of 120-130° C. and sent to the reactor. In addition, nitrogen gas was also supplied into the reactor in an amount of 5-600 mol % relative to the amount of raw material supplied.
The reaction of hexafluorobenzene (C6F6) with the fluorinating agent prepared according to the above-described method was carried out under the following reaction conditions.
Reaction Conditions:
After the hexafluorobenzene was fluorinated under the above-described conditions, the resulting gas was condensed using both trap of ice water and trap of acetone/liquid nitrogen slush. Then, the reaction product was analyzed using gas chromatography. The analysis results are shown in Tables 1 and 2 below.
Examples 5 to 9 were carried out according to the reaction conditions shown in Tables 1 and 2 in the same manner as in Examples 1 to 4, except that the compositions and contents of the fluorinating agent were changed. The results are shown in Tables 1 and 2 below.
In the results shown in Tables 1 and 2 above, as the ratio of CoF3 had increased, the conversion of C6F6 was increased, but the selectivity of C6F10 was decreased. Under optimal reaction condition, the selectivity of C6F10 could reach about 99%.
In the present invention, the two reactors A and B are connected in parallel and used alternately. Specifically, when the reaction in one reactor is completed, the remaining organic product is discharged with nitrogen, and then fluorine gas is introduced into the reactor to activate the fluorinating agent. At the same time, in the other reactor which is standing by, the reaction of the organic material with the fluorinating agent is initiated. For commercial application, the reaction must be continuously carried out, and thus two reactors are alternatively used in order for the process of activating the fluorinating agent and the reaction process to be repeatedly carried out.
As described above, the process of the present invention has an advantage in that decafluorocyclohexene can be prepared with a selectivity of more than 99%.
Although the preferred embodiment of the present invention has been described for illustrative purposes, those skilled in the art will appreciate that various modifications, additions and substitutions are possible, without departing from the scope and spirit of the invention as disclosed in the accompanying claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2008-0112622 | Nov 2008 | KR | national |
