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Method for preparing pentafluoroethane

A pentafluoroethane and pentachloroethane technology, which is applied in the field of pentafluoroethane preparation, can solve problems such as tetrachloroethylene is easy to form carbon, pentafluoroethane has no competitive advantage, and equipment corrosion, so as to avoid adverse effects 、Solve the effect of high raw material cost and operating cost

Active Publication Date: 2011-05-11
CHANGSHU 3F FLUOROCHEM IND CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the high manufacturing cost of tetrafluoroethylene, pentafluoroethane produced by the tetrafluoroethylene route has almost no competitive advantage in the market, but unfortunately, this process route is almost always used in China
The process route of direct gas-phase fluorination of tetrachloroethylene as raw material to produce pentafluoroethane, because olefins directly enter the gas-phase catalyst, the catalyst is prone to failure, and at the temperature of gas-phase fluorination, tetrachloroethylene is easy to form carbon, so further accelerated catalyst failure
Therefore, although the raw material cost of tetrachlorethylene is low, its operating cost is high, and the equipment is seriously corroded.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] exist Put the quartz tubular reactor under ultraviolet light, and raise the temperature inside the tube to 100°C, ready to start the feeding reaction. After trichlorethylene is mixed with chlorine, drop into tubular reactor, the feed rate of trichlorethylene is 3945 grams / hour, and the feed rate of chlorine is 2343 grams / hour. The product of trichlorethylene and chlorine in the tubular reactor is directly washed with water and alkali, and rectified to obtain pentachloroethane with a purity of 99.0%. The charging amount of pentachloroethane per hour is 5908 grams, and the yield of pentachloroethane is 97.25%.

[0027] exist The stainless steel tubular reactor is filled with 5 kg of catalyst, which contains 2550 grams of aluminum fluoride, 250 grams of potassium fluoride, 2000 grams of chromium fluoride and 200 grams of cobalt fluoride. Warm up to 400°C with N 2 The catalyst was activated for 10 hours and then cooled to 300°C. After pentachloroethane and hydrogen f...

Embodiment 2

[0030] exist Put the quartz tubular reactor under ultraviolet light, and raise the temperature in the tube to 120°C, ready to start the feeding reaction. After trichlorethylene is mixed with chlorine, drop into tubular reactor, the feed rate of trichlorethylene is 3945 grams / hour, and the feed rate of chlorine is 2556 grams / hour. The product of trichlorethylene and chlorine in the tubular reactor is directly washed with water and alkali, and rectified to obtain pentachloroethane with a purity of 99.4%. The charging amount of pentachloroethane per hour is 6001 grams, and the yield of pentachloroethane is 98.78%.

[0031] exist The stainless steel tubular reactor is filled with 5 kg of catalyst, which contains 2400 grams of aluminum fluoride, 150 grams of potassium fluoride, 1200 grams of chromium fluoride and 1250 grams of cobalt fluoride. Warm up to 400°C with N 2 The catalyst was activated for 10 hours and then cooled to 320°C. After pentachloroethane and hydrogen fluo...

Embodiment 3

[0034] exist Put the quartz tubular reactor under ultraviolet light, and raise the temperature in the tube to 130°C, ready to start the feeding reaction. After trichlorethylene is mixed with chlorine, drop into tubular reactor, the feed rate of trichlorethylene is 3945 grams / hour, and the feed rate of chlorine is 2769 grams / hour. The product of trichlorethylene and chlorine in the tubular reactor is directly washed with water and alkali, and rectified to obtain pentachloroethane with a purity of 99.0%. The charging amount of pentachloroethane per hour is 5413 grams, and the yield of pentachloroethane is 89.10%.

[0035] exist The stainless steel tubular reactor is filled with 5 kg of catalyst, which contains 2550 grams of aluminum fluoride, 250 grams of potassium fluoride, 2000 grams of chromium fluoride and 200 grams of cobalt fluoride. Warm up to 400°C with N 2 The catalyst was activated for 10 hours and then cooled to 330°C. After pentachloroethane and hydrogen fluor...

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PUM

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Abstract

The invention discloses a method of preparing Pentafluoroethane. Chlorylene and chlorine gas act addition reaction under the ultraviolet light catalysis to prepare pentachloroethane; the pentachloroethane reacts with fluorine hydride through the catalysis of a catalyst to prepare trifluoro dichloroethane; the trifluoro dichloroethane reacts with the fluorine hydride through the catalysis of the catalyst to generate the Pentafluoroethane. The method of preparing Pentafluoroethane is that the chlorylene is adopted to generate the pentachloroethane which enters into gas phase for fluorizating toobtain the Pentafluoroethane, thereby preventing olefins from directly entering into the gas phase for fluorizating to cause harmful effects, fundamentally solving the difficult problems that the material cost and the operation cost are on high side in the original Pentafluoroethane technology, and providing a new technology route to the preparation of the Pentafluoroethane.

Description

technical field [0001] The invention relates to a preparation method of chemical products, in particular to a preparation method of pentafluoroethane (HFC125). Background technique [0002] Pentafluoroethane (HFC125) has an ozone destruction coefficient of 0 and is currently used as a substitute for chlorodifluoromethane (HCFC22) and is widely used in the field of refrigeration. At present, the global annual output is about 60,000 tons, and the main production route uses tetrafluoroethylene or tetrachloroethylene as the main raw material. Such as document US5399549, CN1035812, CN1308596, CN1273577, US5300711, US5300710 etc. all are the processing route with tetrachloroethylene or tetrafluoroethylene as main raw material. Due to the high manufacturing cost of tetrafluoroethylene, pentafluoroethane produced by the tetrafluoroethylene route has almost no competitive advantage in the market, but unfortunately, this process is almost always used in China. The process route of d...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C19/08C07C17/04
Inventor 司林旭张平忠徐建林张建平
Owner CHANGSHU 3F FLUOROCHEM IND CO LTD