Method for preparing cyclopentane refrigerant
A refrigerant and cyclopentane technology, applied in chemical instruments and methods, purification/separation of hydrocarbons, hydrocarbons, etc., can solve the problem that cyclopentane and 2,2-dimethylbutane cannot be separated and are not applicable Industrial production, narrow operating range, etc., to achieve the effect of high selectivity, good stability, and low solvent ratio
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Embodiment 1
[0018] The composition of raw materials is as follows:
[0019]
[0020] Weigh 1000g of raw oil to remove n-pentane and isopentane components under the conditions of operating pressure of 102KPa, reflux ratio of 4.5, and tower bottom temperature of 65°C, and then remove n-pentane and isopentane components at an operating pressure of 110KPa and a reflux ratio of 12 , under the condition that the temperature at the bottom of the tower is 78°C, the carbon six components are removed, and the main components are a mixture of cyclopentane and 2,2-dimethylbutane, and the purity of cyclopentane is 90.1%; controlled extractive distillation The operating pressure of the tower is 102KPa. Weigh a certain amount of the mixture and acetonitrile to carry out extractive distillation experiment, wherein the mass ratio of the mixture to acetonitrile is 1:6, the reflux ratio is 70, the temperature at the bottom of the tower is 70°C, and the mixture containing cyclopentane is obtained at the bo...
Embodiment 2
[0022] The composition of raw materials is as follows:
[0023]
[0024] Weigh 1000g of feedstock oil to remove n-pentane and isopentane components under the conditions of operating pressure of 110KPa, reflux ratio of 4, and tower bottom temperature of 68°C, and then remove n-pentane and isopentane components at an operating pressure of 102KPa and a reflux ratio of 9 , under the condition that the temperature at the bottom of the tower is 75°C, the C6 components are removed, and the main components are a mixture of cyclopentane and 2,2-dimethylbutane, and the purity of cyclopentane is 91.2%; controlled extractive distillation The operating pressure of the tower is 115KPa. Weigh a certain amount of the mixture and acetonitrile for extractive distillation experiment, wherein the mass ratio of the mixture to acetonitrile is 1:8, the reflux ratio is 55, the temperature at the bottom of the tower is 78°C, and the mixture containing cyclopentane is obtained at the bottom of the to...
Embodiment 3
[0026] The composition of raw materials is as follows:
[0027]
[0028] Weigh 1000g of raw oil to remove n-pentane and isopentane components under the conditions of operating pressure of 120KPa, reflux ratio of 5, and tower bottom temperature of 75°C, and then remove n-pentane and isopentane components at an operating pressure of 115KPa and a reflux ratio of 11 , under the condition that the temperature at the bottom of the tower is 80°C, the carbon six components are removed, and the main components are a mixture of cyclopentane and 2,2-dimethylbutane, and the purity of cyclopentane is 92.3%; controlled extractive distillation The operating pressure of the tower is 120KPa. Weigh a certain amount of the mixture and acetonitrile to carry out the extractive distillation experiment, wherein the mass ratio of the mixture to acetonitrile is 1:9, the reflux ratio is 45, the temperature at the bottom of the tower is 80°C, and the mixture containing cyclopentane is obtained at the ...
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