A method for comprehensive utilization of olefins in Fischer-Tropsch synthesis light distillate oil
A technology of light distillate oil and Fischer-Tropsch synthesis, which is applied in distillation purification/separation, preparation of ether by addition of unsaturated compounds, preparation of ether, etc. It can solve problems such as air pollution, reduce consumption, and alleviate the contradiction between supply and demand.
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Embodiment 1
[0028] Fischer-Tropsch light C5 distillate oil 1 enters an extractive distillation tower with a theoretical plate number of 74, the extraction agent selected is N, N-dimethylformamide (DMF), the reflux ratio is 8.5, and the feed position is (from From top to bottom, the same below) 3 and 20, a stream 3 rich in 1-pentene is obtained from the top of the extractive distillation tower, and a stream 6 of extractant and raffinate carbon five components is obtained from the bottom of the extractive distillation tower; The weight ratio of the raw material to the extractant is 15:1, the feed temperature of the extractant is 20°C, the temperature at the top of the tower is 25°C, the temperature at the bottom of the tower is 55°C, and the operating pressure is normal pressure.
[0029] The stream 3 enters a precision rectification tower with a theoretical plate number of 214, the reflux ratio is 10.54, and the feed position is 152, and the 1-pentene refined stream 4 can be obtained from t...
Embodiment 2
[0038] Fischer-Tropsch light C5 distillate oil 1 enters the extractive distillation tower with a theoretical plate number of 74. The extraction agent selected in this implementation case is N,N-dimethylformamide (DMF), the reflux ratio is 9, and the feed The positions are (from top to bottom, the same below) 3 and 20, the stream 3 rich in 1-pentene is obtained from the top of the extractive distillation tower, and the extractant and raffinate carbon five components are obtained from the bottom of the extractive distillation tower The stream 6; the weight ratio of the raw material and the extractant is 20:1, the feed temperature of the extractant is 30°C, the temperature at the top of the tower is 40°C, the temperature at the bottom of the tower is 70°C, and the operating pressure is normal pressure.
[0039] The stream 3 enters a precision rectification tower with a theoretical plate number of 178, a reflux ratio of 13, and a feed position of 126, and the refined stream 4 of 1-...
Embodiment 3
[0048] Fischer-Tropsch light C5 distillate oil 1 enters the extractive distillation tower with a theoretical plate number of 74. The extraction agent selected in this implementation case is N, N-dimethylformamide (DMF), the reflux ratio is 10, and the feed The positions are (from top to bottom, the same below) 3 and 20, the stream 3 rich in 1-pentene is obtained from the top of the extractive distillation tower, and the extractant and raffinate carbon five components are obtained from the bottom of the extractive distillation tower The stream 6; the weight ratio of the raw material and the extractant is 18:1, the feed temperature of the extractant is 25°C, the temperature at the top of the tower is 30°C, and the temperature at the bottom of the tower is 60°C.
[0049] The stream 3 enters a precision rectification tower with a theoretical plate number of 162, the reflux ratio is 15, and the feed position is 115, and the refined stream 4 of 1-pentene can be obtained from the top ...
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