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Preparation method of 1,2,3,3,3-pentafluoropropylene
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A technology of pentafluoropropylene and hexafluoropropylene, applied in the field of dehydrofluorination to obtain 1, which can solve the problems of difficult acquisition of CFC-1213xa and low single-pass total yield
Active Publication Date: 2012-10-10
XIAN MODERN CHEM RES INST
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Problems solved by technology
But this synthesis method exists the problem that raw material CFC-1213xa is not easy to obtain, and the total yield of one pass is low
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Embodiment 1
[0037] 50 ml of a commercially available 2% Pd / C catalyst was added to a carbon steel pipe with an inner diameter of 38 mm. The temperature of the first reactor is 50°C, and H 2 and HFP, control H 2 The molar ratio to HFP is 2, and the space velocity of HFP is 360h -1 , reaction pressure 0.1MPa, after reacting for 20h, use gas chromatography to analyze the composition of organic matter in the reaction product, the results are shown in Table 1.
Embodiment 2
[0039] Add 50 ml of a commercially available 5% Pd / C catalyst into a glass tube with an inner diameter of 38 mm. The first reactor was placed in an ice bath at 0°C, and H 2 and HFP, control H 2 The molar ratio to HFP is 2, and the space velocity of HFP is 480h -1 , reaction pressure 0.1MPa, after reacting for 20h, use gas chromatography to analyze the composition of organic matter in the reaction product, the results are shown in Table 1.
Embodiment 3
[0041] The operation was basically the same as in Example 1, except that the reaction temperature was 100°C. The results are shown in Table 1.
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Abstract
The invention discloses a preparation method of Z-1,2,3,3,3-pentafluoropropylene (Z-HFO-1225ye), which comprises the following steps: a. adding hydrogen and hexafluoropropylene into a first reactor and reacting under the existence of a hydrogenation catalyst; b. leading a product prepared in the step a to flow into a first distillation tower for separation and returning a tower component to the first reactor; c. adding N2 and a tower reactor component 1,1,2,3,3-hexafluoropropane (HFC-263ea) prepared in the step b into a second reactor and reacting the 1,1,2,3,3-hexafluoropropane under the existence of off hydrogen fluoride and isomerization catalysts; d. leading a product prepared in the step c to flow into a second distillation tower for separation and returning a tower component into the second reactor; e. adding a tower reactor component prepared in the step d into a third distillation tower for separation and separating the tower component with a system to obtain the target product Z-HFO-1225ye after treatment; and f. adding a tower reactor component prepared in the step e into a phase separator for phase separation, returning an organic phase with rich HFC-236es into the second reactor and separating an organic phase with rich HF from the system. The invention is mainly used for the preparation of the Z-HFO-1225ye.
Description
technical field [0001] The present invention relates to a preparation method of 1,2,3,3,3-pentafluoropropene (HFO-1225ye), in particular to a method of using hydrogen and hexafluoropropylene (HFP) as raw materials, first in the presence of a hydrogenation catalyst Hydrogenation, and then dehydrofluorination under the action of a dehydrofluorination catalyst to obtain 1,2,3,3,3-pentafluoropropene. Background technique [0002] 1,2,3,3,3-Pentafluoropropene (HFO-1225ye), with low greenhouse effect potential (GWP) and zero ozone depletion potential (ODP), is considered to be the most potential alternative to 1,1 , a third-generation ODS substitute for 1,2-tetrafluoroethane (HFC-134a), widely used as a refrigerant, blowing agent, aerosol propellant, solvent, etc. [0003] The world patent WO2007019354A discloses a method for synthesizing HFO-1225ye by dehydrofluorination. The method uses 1,1,1-trifluoro-2,3,3-trichloropropene (CFC-1213xa) as a raw material for a three-step reac...
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