Separation method of 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene
A technology for tetrafluoropropane and trifluoropropene is applied in the field of separation of 2-chloro-1,1,1,2-tetrafluoropropane, which can solve the problems of increasing equipment, operators and environmental hazards, and achieve a green separation process. Safe, easy to implement, and simple to operate
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Embodiment 1
[0024]Both the extractive distillation tower T1 and the extraction recovery tower T2 are packed towers with a diameter of Φ25mm and Φ3×3θ ring stainless steel packing inside, and the height of the packing layer is 4m. The rectification material 1 is the crude product of synthetic 2-chloro-1,1,1,2-tetrafluoropropane, wherein the mass percentage of HCFC-244bb is 90%, and the mass percentage of HCFO-1233xf is 10%. The material 1 is fed from the middle part of the extractive distillation tower T1, and the flow rate is 100g / h, and the bottom distillate 5 of the T2 tower (that is, the circulating extractant, N, N-dimethylformamide) is fed from the upper part of the T1 tower, The flow rate is 400g / h, T1 overhead distillate 2 is HCFC-244bb product, T1 tower still distillate 3 is HCFO-1233xf and extractant, and enters the extraction recovery tower T2 tower. T2 overhead distillate 4 is HCFO-1233xf product, and T2 tower still distillate 5 is extractant, which is returned to T1. See Tabl...
Embodiment 2
[0030] The operating process of Example 2 is similar to that of Example 1, except that the operating parameters of the rectifying towers T1 and T2 are different. The operating parameters are shown in Table 3, and the stream composition of Example 2 is shown in Table 4.
[0031] Tower operation condition in the embodiment 2 of table 3
[0032] Distillation column
T1
T2
Operating pressure / kPa(A)
200
100
Tower top temperature / ℃
34.1
12.2
Tower kettle temperature / ℃
168
152.2
Reflux ratio
5
20
[0033] The logistics composition in the embodiment 2 of table 4
[0034]
Embodiment 3
[0036] The operation process of embodiment 3 is similar to embodiment 1, and the difference is that the composition of material (1) becomes HCFC-244bb85%, HCFO-1233xf 5%, and the extractant browsing is adjusted to 1000g / h, and operating parameters are shown in Table 5, The logistics composition of embodiment 3 is shown in table 6.
[0037] Tower operation condition in the embodiment 3 of table 5
[0038] Distillation column
T1
T2
Operating pressure / kPa(A)
200
100
Tower top temperature / ℃
34.1
12.1
Tower kettle temperature / ℃
174.4
152.2
Reflux ratio
5
20
[0039] The logistics composition in the embodiment 3 of table 6
[0040]
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Abstract
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