Preparation method of Z-1,1,1,4,4,4-hexafluoro-2-butene
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A Z-2, Z-1 technology, applied in Z-1, can solve the problems of pollution, corrosion, serious pollution, etc.
Active Publication Date: 2016-10-12
泉州宇极新材料科技有限公司
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There are following defects in these routes: firstly, various literatures do not list the single-pass yield data of Z-1,1,1,4,4,4-hexafluoro-2-butene, and the yields given are generally The sum of the yields of Z-1,1,1,4,4,4-hexafluoro-2-butene and E-1,1,1,4,4,4-hexafluoro-2-butene, generally The yield of Z-1,1,1,4,4,4-hexafluoro-2-butene in the method is very low, while E-1,1,1,4,4,4-hexafluoro-2-butene Alkenes are very high; secondly, 1,2-dichloro-1,1,4,4,4-pentafluorobutane, 2-chloro-1,1,1,4,4,4-hexafluorobutane Or 1,1,1-trifluoro-2-bromo-2-chloroethane is the defect that the raw material price is expensive and difficult to obtain in the route of starting raw material; With 1,1-dichloro-3,3,3-three The coupling route with fluoroethane as the starting material produces a large amount of waste liquid that is difficult to recycle, and the resulting pollution is very serious; the route of hexafluoropropylene as the starting material is relatively long, and hexafluoropropylene is difficult to transport, and there is detonation. The danger of hexachlorobutadiene is that the route of starting raw material is corroded seriously, pollutes serious problem, and wherein the liquid phase system that antimony pentachloride or titanium tetrachloride and HF forms is very strong to the corrosion of equipment, and Pollution is also very serious
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Embodiment 1
[0063] Preparation of fluorination catalyst: Dissolve chromium nitrate in water, add precipitant ammonia water at 60°C, control the pH of the solution between 7.5 and 8.5, make it fully precipitate under stirring conditions, filter the formed slurry, and use Wash with ion water until neutral, then dry at 150°C for 12 hours to obtain chromium hydroxide. According to the mass percentages of tetravalent chromium ions and iron elements being 95% and 5%, the above-mentioned chromium hydroxide and iron hydroxide are uniformly mixed, pressed and molded to obtain a catalyst precursor, and then the catalyst precursor is placed in a nitrogen atmosphere. After calcination at 450°C for 10 hours, activate at 300°C with a mixed gas of hydrogen fluoride and hydrogen at a molar ratio of 10:1 for 10 hours, and at 300°C with a mixed gas atmosphere of chlorine and nitrogen with a molar ratio of 1:10 Oxidation for 12 hours to obtain a fluorination catalyst.
[0064] A tubular reactor made of Inc...
Embodiment 2
[0066] The same operation as in Example 1, the difference is that "according to the mass percentage of tetravalent chromium ion and iron element is 95% and 5%, the chromium hydroxide and iron hydroxide are mixed homogeneously" to "according to the tetravalent The mass percent composition of chromium ion and zinc element is 95% and 5%, chromium hydroxide and zinc hydroxide are mixed " homogeneously ", and the chlorine that oxidizes the catalyst is changed into the oxygen of the amount of equal substance, the result is shown in the table 1.
Embodiment 3
[0068] The same operation as in Example 1, the difference is that the ferric hydroxide in the fluorination catalyst precursor is changed to zinc hydroxide of equal quality and the chlorine gas that is oxidized to the catalyst is changed to the ozone of the amount of the same substance, the results are shown in Table 1.
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Abstract
The invention relates to a preparation method of Z-1,1,1,4,4,4-hexafluoro-2-butene, belonging to the field of chemical synthesis. The method comprises the following steps of taking hexachlorobutadiene (HCBD) as a raw material, performing gas-phase catalytic chlorination-fluoridation separation to obtain 2,3-dichlorohexafluoro-2-butene, performing liquid-phase dechlorination to obtain hexafluoro-2-butyne, and preparing the Z-1,1,1,4,4,4-hexafluoro-2-butene (Z-HFO-1336mzz) by means of performing gas-phase catalytic hydrogenation, wherein three reactions are included totally. The Z-1,1,1,4,4,4-hexafluoro-2-butene with high selectivity is obtained by means of performing catalytic hydrogenation by adopting the hexafluoro-2-butyne, and meanwhile the product is easily separated from side products and the raw material. The method disclosed by the invention has the advantages that the original raw material is easily obtained, the activity of a catalyst is high, the service life of the catalyst is long, the raw material can be recycled, and the standard of zero emissions is reached.
Description
technical field [0001] The present invention relates to a preparation method of Z-1,1,1,4,4,4-hexafluoro-2-butene (Z-HFO-1336mzz), in particular to a method starting with hexachlorobutadiene Raw materials, chlorofluorination reaction in the presence of fluorination catalyst first, then dechlorination reaction in the presence of zinc powder, and finally hydrogenation in the presence of hydrogenation catalyst to obtain Z-1,1,1,4,4,4-hexa Process for the preparation of fluoro-2-butene. Background technique [0002] Z-1,1,1,4,4,4-hexafluoro-2-butene (Z-HFO-1336mzz), with low greenhouse effect potential (GWP) and zero ozone depletion potential (ODP), It is considered to be an ideal substitute with the most potential to replace 1,1-dichloro-1-fluoroethane (HCFC-141b), and can be used as a refrigerant, blowing agent, fire extinguishing agent, etc. [0003] U.S. Patent US5463150 reported that in sulfolane solvent, 190 ° C, 1,2-dichloro-1,1,4,4,4-pentafluorobutane or 2-chloro-1,1,1...
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