专利摘要:
A graphite fluoride comprising mainly poly-dicarbon monofluoride represented by the formula (C2F)n can be produced in an extremely short period of time by a process comprising reacting a graphite material with fluorine in the presence of a specific fluoride.
公开号:SU1190982A3
申请号:SU823381403
申请日:1982-01-27
公开日:1985-11-07
发明作者:Ватанабе Нобуацу;Накадзима Цуеси;Кавагути Масаюки
申请人:Эпплайд Сайенс Рисерч Институт И Нобуацу Ватанабе (Фирма);
IPC主号:
专利说明:

The invention relates to methods for producing graphite fluoride, recommended for use as an active material in electrical cells, lubricants, water resistant staining to water and / or oil repellent, etc. The method of obtaining graphite fluoride is known (Formulas C P by processing graphite using a pro- 500 c Ij However, this method is very sophisticated. The purpose of the invention is to reduce the duration of the process. The goal is achieved by the fact that according to the method of processing graphite powder fluorine at 300-500 ° C, the treatment is carried out in the presence of fluoride of an element selected from the group consisting of lithium, magnesium, calcium, aluminum, chromium, manganese, cobalt, iron, copper and zinc. Graphite and fluoride of the selected element contacted with fluorine at a temperature of from room temperature to 100 ° C and then heated to 300-500 ° C. Contact with fluorine is carried out for min-20h, anheating is up to 300-500 ° C with a speed of 2-100 degrees / mic Typically fluorite is graphite to achieve a constant weight of the product. In the presence of lithium, magnesium, kalidium, aluminum, chromium, manganese, cobalt, iron, copper, or zinc fluorides, the reaction is significantly accelerated. Contacting graphite and fluoride of an element with fluorine and subsequent heating under these conditions will further intensify the process. In this case, the deviation from these modes leads to a slowing down of the fluorination process. The separation of graphite fluoride produced from the use of fluoride elements is carried out, for example, in water, by the method according to the flotation method, since (Cj, F) has water-repellent properties. When using fluoride gas, separation is easier. Example 1. A mixture of 50 mg of Madagascar flake natural graphite with a particle size of 16 (0.991 mm) or more and 50 mg of AlFg is placed into a monel reactor. Fluorine is introduced into the reactor at room temperature and a pressure of 760 mm Hg. (the time of introduction of fluorine is 5 minutes), the reaction system is heated to 400 ° C at a temperature rise rate of 30 K / min. At this temperature, the reaction continues for 5 hours. Graphite fluoride is obtained, which is gray in color and has an F / C ratio of 0.677, with a yield of 100% relative to the used graphite. Example 2. Preparation of graphite fluoride is carried out analogously to example 1, except that after the introduction of fluorine, the reaction system is heated to 100 ° C, held for 0.5 h, and then heated to 400 ° C at a rate of 2.5 degrees / min At 400 ° C, the reaction is continued for 9 hours. Gray graphite fluoride is obtained with an F / C ratio of 0.601 and a yield of 100% relative to the graphite used. Sample S-13 and 18-25 and comparative example 4. The preparation of graphite fluoride is carried out analogously to example 2. The particle size of graphite, the type of fluoride element introduced, the contact and reaction times and the heating rate are changed to 300-500 0. The process data are shown in the table. Comparative example 1. The process is carried out analogously to example 1 except that. That AIF is not used. After VOh after the start of the reaction at 400 ° С, the product is examined by x-ray diffraction. In the powder X-ray diffraction pattern, a peak is still observed, due to the remaining unreacted carbon. Two weeks after the start of the reaction, graphite fluoride was obtained with an F / C ratio of 0.62, Examples 14-17 and Comparative Examples 2 and 3. The preparation of fluoride and graphite was carried out analogously to Example 2, except that heat-treated petroleum coke (Franklin number, 31, heat treatment at 2 for 30 minutes) with a particle size of 46 μm is used instead of natural graphite and the process conditions are changed. Graphite fluoride is obtained having an F / C ratio according to the table. The use of the invention makes it possible to shorten the process for producing graphite fluoride of the formula () by two or more times as compared with the known method.
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权利要求:
Claims (3)
[1]
1. THE METHOD FOR PRODUCING GRAPHITE FLUORIDE of the formula (C 2 F) n , including the treatment of graphite powder with fluorine at 300-500 ° C, is distinguished by the fact that, in order to reduce the duration of the process, the treatment is carried out in the presence of fluoride of the element selected from the group consisting of lithium, magnesium, calcium, aluminum, chromium, manganese, cobalt, iron, copper and zinc.
[2]
2. The method of claim 1, wherein the graphite and fluoride of the selected element are contacted with fluorine at a temperature of from room temperature to 100 ° C and then heated to 300500 ° C.
[3]
3. The method according to p. 2, characterized in that the contacting with fluorine is carried out for 1 minute - 20 hours, and heating to 300-500 C at a speed of 2-100 deg / min.
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同族专利:
公开号 | 公开日
JPS6220127B2|1987-05-06|
IT1150602B|1986-12-17|
FR2512429A1|1983-03-11|
IT8219278D0|1982-01-25|
GB2106882A|1983-04-20|
FR2512429B1|1985-10-25|
US4423261A|1983-12-27|
NL8200160A|1983-04-05|
JPS5845104A|1983-03-16|
DE3201116A1|1983-03-17|
GB2106882B|1985-02-06|
DE3201116C2|1987-02-05|
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法律状态:
优先权:
申请号 | 申请日 | 专利标题
JP56143007A|JPS6220127B2|1981-09-10|1981-09-10|
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