System and method for separating methanol-water through rectification coupled membrane
A rectification coupling and separation method technology, which is applied in the field of rectification coupling membrane separation, can solve the problems of high energy consumption, high investment cost, and high separation requirements of multi-tower rectification separation, so as to reduce energy consumption, low investment cost, optimize The effect of process conditions
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Embodiment 1
[0024] In this embodiment, the rectification coupling membrane separation methanol-water system, such as figure 1 Shown, comprise rectifying tower 1, the upper end of described rectifying tower 1 is connected with condenser 2, the lower end of described rectifying tower 1 is connected with reboiler 3, and described condenser 2 is connected with centrifugal pump 4, so The centrifugal pump 4 is connected to the membrane separator 5.
Embodiment 2
[0026] The method for separating methanol-water by the system in Example 1 is adopted in the present embodiment, comprising the following steps:
[0027] S1, feed the mixture of methanol and water into the rectification tower 1, separate most of the water from the bottom of the rectification tower 1, and steam the mixed gas of residual water and methanol from the top outlet of the rectification tower 1, the said The number of trays of the rectification tower 1 is 9, and the reflux ratio is 0.18. The feed position of the mixture of methanol and water is the 7th tray of the rectification tower 1, and the temperature of the rectification tower 1 top is 68.22°C, the temperature of the bottom of the rectification tower 1 is 88.97°C, the working pressure of the rectification tower 1 is 120Kpa, and the pressure drop of the single plate is 0.7KPa;
[0028] The mixture of methanol and water in S1 is composed of methanol with a mass fraction of 57.1% and water with a mass fraction of 42...
Embodiment 3
[0033] The method for separating methanol-water by the system in Example 1 is adopted in the present embodiment, comprising the following steps:
[0034] S1, feed the mixture of methanol and water into the rectification tower 1, separate most of the water from the bottom of the rectification tower 1, and steam the mixed gas of residual water and methanol from the top outlet of the rectification tower 1, the said The number of trays of the rectification tower 1 is 9, and the reflux ratio is 0.39. The feed position of the mixture of methanol and water is the 7th tray of the rectification tower 1, and the temperature of the top of the rectification tower 1 is 67.22°C, the temperature of the bottom of the rectification tower 1 is 91.53°C, the working pressure of the rectification tower 1 is 120Kpa, and the pressure drop of the single plate is 0.7KPa;
[0035] The mixture of methanol and water in S1 is composed of methanol with a mass fraction of 57.1% and water with a mass fractio...
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