Azeotrope-like compositions of 1,1,3,3-pentafluorobutane
A kind of technology of pentafluorobutane composition, applied in the field of binary azeotrope-like composition
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Embodiment 1
[0093] Example 1: Effect of Steam Leakage on Steam Pressure
[0094]The initial composition was charged into a container at a temperature of 40°C and the vapor pressure of the composition was measured. The composition was allowed to leak from the container while maintaining a constant temperature of 40°C until 50% by weight of the initial composition was removed, at which point the vapor pressure of the remaining composition in the container was measured. The results are summarized in Table 1 below.
[0095] composition
[0096] The results of this example indicate that these compositions are azeotrope-like compositions, since when 50% by weight of the initial composition is removed, the difference in vapor pressure of the remaining composition at 40°C from the vapor pressure of the initial composition is within about 10% or less. Also, in some cases, the pressure of a given composition is higher than the vapor pressure of any of the pure components in the compos...
Embodiment 2
[0097] Example 2: Distillation
[0098] A solution containing 30.0% by weight of HFC-43-10mee and 70.0% by weight of HFC-365mfc was prepared in a suitable container and mixed thoroughly. The solution was distilled on a five-stage Oldershaw distillation column (7 cm diameter, 40 cm high) using a reflux:draw ratio of 10:1. Top and bottom temperature readings are accurate to 1°C. Distillation was performed at a pressure of 760 mmHg. Distillate composition was determined by gas chromatography. The results are listed in Table 2.
[0099] distillate
[0100] Analysis of the above data shows only small differences in overhead temperature and distillate composition as the distillation proceeds, exhibiting azeotrope-like properties.
Embodiment 3
[0101] Example 3: Distillation
[0102] A solution containing 26.7% by weight of HFC-43-10mee, 44.7% by weight of HFC-365mfc and 28.6% by weight of tDCE was prepared in a suitable container and mixed thoroughly. The solution was distilled on a five-stage Oldershaw distillation column (7 cm diameter, 40 cm high) using a reflux:draw ratio of 10:1. Head and kettle temperature readings are accurate to 1°C. Distillation was performed at a pressure of 757.53 mmHg. Distillate composition was determined by gas chromatography. The results are listed in Table 3.
[0103] distillate
[0104] Analysis of the above data shows only small differences in overhead temperature and distillate composition as the distillation proceeds, exhibiting azeotrope-like properties.
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