Method for separating 1-butylene
A technology of butene and absorption tower, applied in the field of separating 1-butene, can solve the problems of high energy consumption and high cost, and achieve the effects of less investment in equipment, low production cost, and reduced energy consumption
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Embodiment 1
[0044] Feed gas (see Table 1 for components and their content) enters the stainless steel packed tower with a tower diameter of 20mm and 29 trays from the bottom of the tower at a flow rate of 1429ml / hr. The absorbing liquid is an aqueous solution of silver nitrate, silver nitrate solution The mass percent concentration is 30%, enters the absorption tower from the top of the tower at a flow rate of 50ml / hr, the temperature in the tower is 26°C, the pressure is 0.1MPa, the tail gas is released from the top of the tower, and the absorption liquid flows out from the tower kettle;
[0045] 60 g / hr of the absorption liquid flowing out from the absorption tower tank is introduced into the upper part of the extraction tank, and 110 g / hr of extractant n-hexane is introduced from the upper part of the extraction tank, the temperature of the extraction tower is 28 ° C, and the pressure is 0.1 MPa;
[0046] The gas analyzed from the extract liquid that flows out from the top of the extrac...
Embodiment 2
[0049] Feed gas (see Table 1 for components and their content) enters the stainless steel packed tower with a tower diameter of 20mm and 29 trays from the bottom of the tower at a flow rate of 1429ml / hr. The absorbing liquid is an aqueous solution of silver nitrate, silver nitrate solution The mass percent concentration is 30%, enters the absorption tower from the top of the tower at a flow rate of 50ml / hr, the temperature in the tower is 26°C, the pressure is 0.1MPa, the tail gas is released from the top of the tower, and the absorption liquid flows out from the tower kettle;
[0050] 60 g / hr of the absorption liquid flowing out from the absorption tower tank is introduced into the upper part of the extraction tank, and 60 g / hr of extractant n-heptane is introduced from the upper part of the extraction tank, the temperature of the extraction tower is 28 ° C, and the pressure is 0.1 MPa;
[0051] The gas analyzed from the extract liquid that flows out from the top of the extrac...
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