Production raw material of liquid ventilation fluid and material for ophthalmic surgery and continuous preparation method of production raw material
An ophthalmic surgery and liquid technology, applied in the field of perfluorooctane preparation, can solve the problems of low perfluorooctane yield, low yield, many by-products, etc., and achieves easy control of reaction conditions, easy separation and purification, and no three wastes. The effect of emissions
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Embodiment 1
[0026] A Monel alloy reactor with an inner diameter of 80 mm and a length of 1000 mm is filled with spherical alumina with a diameter of 3 mm. The reactor is heated to 250°C, and a mixed gas of 50% fluorine-50% nitrogen is introduced for fluorination, so that alumina is completely converted into aluminum fluoride. Then the temperature of the reactor is maintained at 200°C, 20% fluorine-nitrogen mixed gas and 10% octane-nitrogen mixed gas are continuously fed in at a molar ratio of fluorine gas to octane 20:1 for reaction, and the residence time is controlled for 5 seconds. After 10 hours, neutralize the collected reaction product with 20% potassium hydroxide aqueous solution to a neutral pH value, and let it stand. After layering, take the organic phase and wash it with deionized water three times. Separate the organic phase and dry it with anhydrous sodium sulfate After rectification and separation, take the fraction with a boiling point of 101-104°C to obtain 1000 g of perflu...
Embodiment 2
[0028] The same equipment as in Example 1 was used. The temperature of the reactor is maintained at 260°C, and 20% fluorine-nitrogen mixed gas and 20% octane-nitrogen mixed gas are continuously fed in at a molar ratio of fluorine gas to octane 20:1 for reaction, and the residence time is controlled for 10 seconds. After 10 hours, neutralize the collected reaction product with 20% potassium hydroxide aqueous solution to a neutral pH value, and let it stand. After layering, take the organic phase and wash it with deionized water three times. Separate the organic phase and dry it with anhydrous sodium sulfate After rectification and separation, take the fraction with a boiling point of 101-104°C to obtain 1500 grams of perfluorooctane with a purity of 99.5% and a yield of about 85%.
Embodiment 3
[0030] The same equipment as in Example 1 was used. The temperature of the reactor was maintained at 280°C, and 20% fluorine-nitrogen mixed gas and 15% octane-nitrogen mixed gas were continuously fed in at a ratio of 25:1 fluorine gas to octane molar ratio for reaction, and the residence time was controlled to be 10 seconds. After 10 hours, neutralize the collected reaction product with 20% potassium hydroxide aqueous solution to a neutral pH value, and let it stand. After layering, take the organic phase and wash it with deionized water three times. Separate the organic phase and dry it with anhydrous sodium sulfate After rectification and separation, take the fraction with a boiling point of 101-104°C to obtain 1600 g of perfluorooctane with a purity of 99% and a yield of about 80%.
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Abstract
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