Method for producing n-decane, n-dodecane and n-tetradecane from polyethylene wax by-production light wax oil
A technology of n-dodecane and n-tetradecane, applied in the field of alkane production, can solve the problems of high equipment investment and long production process route, and achieve the effects of low equipment investment, short production process route and flexible process operation.
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Embodiment 1
[0030] Use a polypropylene filter cloth with a filtration accuracy of 1-3 μm to filter the light wax oil, and the thickness of the polypropylene filter cloth is 1.0 mm.
[0031] The volume is 7m 3 Add 3 tons of light wax oil after filtering in the intermittent rectification tower still of the batch rectification tower, the add-on of light wax oil this moment is 3 / 5 of tower still volume, and the theoretical plate number of batch rectification tower is 20, Start the vacuum system, reduce the pressure of the batch rectification tower to 2.5KPa ~ 2.6KPa, then heat the light wax oil in the kettle, and when the temperature of the tower kettle rises to 90°C, there will be reflux at the top of the tower, and the total reflux operation will be performed first. After 30 minutes to 60 minutes, by adjusting the opening of the reflux and extraction valves, the reflux ratio at the top of the tower was controlled to be 2.5, and the former fraction was extracted. When the gas phase temperatu...
Embodiment 2
[0036] According to the operating steps of Example 1, the composition of the raw materials was changed, and the rest of the process conditions were the same as in Example 1. The test results are shown in Table 2.
[0037] Table 2
[0038]
[0039]
Embodiment 3
[0041] According to the operation steps of Example 1, the gas phase temperature at the top of the tower when controlling the production of n-decane is 73°C to 75°C, and the temperature of the gas phase at the top of the tower when producing n-dodecane is 108°C to 110°C. The gas phase temperature at the top of the tower is 139°C to 141°C at the time of tetraoxane, and the extracted materials at the other gas phase temperatures at the top of the tower all enter the fore distillation tank. All the other process conditions are the same as in Example 1, and the test results are shown in Table 3.
[0042] table 3
[0043]
[0044] According to the comparison of Example 1 and Example 3, it can be seen that when the temperature range of the gas phase at the top of the tower is reduced, the purity of the corresponding separated product increases.
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