Method for condensing water-soluble organic matter and device for condensing water-soluble organic matter
A method and a device for condensing a water-soluble organic matter, which can collect a highly concentrated water-soluble organic matter, save energy, and reduce cost of the device by reducing a membrane area. According to the present invention, the permeability ratio of a vapor-permeation separation membrane disposed at least immediately before a final outlet on a non-permeation side in the separation membrane device is lower than those of the other vapor-permeation separation membranes while a hybrid process combining distillation by the distillation column with membrane separation by the separation membrane devices including a plurality of vapor-permeation separation membranes is used and energy saving performance is maintained. Therefore, a highly concentrated and condensed component of a water-soluble organic matter is obtained. In addition, it is possible to reduce a membrane area of the vapor-permeation separation membranes in the whole separation membrane devices and to provide a technology leading to cost reduction.
1. A method for condensing a water-soluble organic matter by distillation and membrane separation, comprising:
distilling a raw material wherein said raw material includes a mixture of water and a water-soluble organic matter having a lower boiling point than water or a mixture of water and a water-soluble organic matter which forms an azeotrope with water and the azeotrope of which with water has a lower boiling point than water, said distillation producing a column top vapor after inputting the raw material into a distillation column; and
introducing said column top vapor obtained in the distillation step into a separation membrane device comprising a first separation membrane device and a second separation membrane device as a subsequent stage thereof, each of the first separation membrane device and the second separation membrane device having a plurality of stages of vapor-permeation separation membranes through which water vapor goes selectively, and obtaining the water-soluble organic matter having a required concentration of more than 99.0% by mass from a final outlet on a non-permeation side in the separation membrane device comprising the first separation membrane device and the second separation membrane device by membrane separation of the vapor-permeation separation membrane, wherein in the vapor-permeation separation membranes of the second separation membrane device, when the permeability of water is referred to as K —W mol/m 2 ·Pa·s and the permeability of the water-soluble organic matter is referred to as K —A mol/m 2 ·Pa·s in the vapor-permeation separation membrane, the permeability ratio K —W /K —A of a vapor-permeation separation membrane disposed at least immediately before the final outlet on the non-permeation side in the separation membrane device comprising the first separation membrane device and the second separation membrane device is lower than those of the other vapor-permeation separation membranes, and wherein the vapor-permeation separation membrane disposed at least immediately before the final outlet on the non-permeation side in the separation membrane device has a portion having a minimum membrane area in a range of the permeability ratio of 50 to 100.
2. The method for condensing a water-soluble organic matter according to claim 1 , wherein the vapor-permeation separation membrane having a lower permeability ratio than the other vapor-permeation separation membranes is disposed in a predetermined range of ⅛ to ½ from the final outlet on the non-permeation side in the separation membrane device of the whole of the plurality of stages of vapor-permeation separation membranes.
3. The method for condensing a water-soluble organic matter according to claim 1 , wherein the vapor-permeation separation membrane having a lower permeability ratio than the other vapor-permeation separation membranes condenses a water-soluble organic matter in the separation membrane device from an intermediate concentration of 99.0% by mass or more to the required concentration.
4. The method for condensing a water-soluble organic matter according to claim 1 , wherein the vapor-permeation separation membrane having a lower permeability ratio than the other vapor-permeation separation membranes has a higher permeability of water than those of the other vapor-permeation separation membranes.
5. The method for condensing a water-soluble organic matter according to claim 1 , wherein at least a part of permeation components of the separation membrane device is introduced into the distillation column.
6. The method for condensing a water-soluble organic matter according to claim 1 , wherein the required concentration of the water-soluble organic matter obtained from the final outlet on a non-permeation side in the separation membrane device comprising the first separation membrane device and the second separation membrane device is 99.9% by mass or more.
7. The method for condensing a water-soluble organic matter according to claim 1 , wherein the water-soluble organic matter is at least one selected from the group consisting of isopropanol, ethanol, methanol, and butanol.
8. The method for condensing a water-soluble organic matter according to claim 1 , wherein the permeability ratio K —W /K —A of the vapor-permeation separation membrane disposed at least immediately before the final outlet on the non-permeation side in the separation membrane device comprising the first separation membrane device and the second separation membrane device is 50 to 200 and the permeability ratio K —W /K —A of the other vapor-permeation separation membranes are 200 to 500.