Membrane distillation module and membrane distillation apparatus using same
The purpose of the present invention is to provide: a membrane distillation module with excellent stability of water treatment ability over time as a result of wetting being controlled; and a membrane distillation apparatus comprising the same. Provided is a membrane distillation module that comprises a housing and multiple porous hollow fiber membranes, both ends of which are bonded and fixed to the housing, wherein: the water contact angle of the outer surfaces of the porous hollow fiber membranes is at least 90°; and a hydrophobic polymer adheres to at least some of the areas of the porous hollow fiber membranes that are not bonded and fixed.
1. A module for membrane distillation comprising a housing, and a plurality of porous hollow fiber membranes each having both ends adhesively anchored to the housing, wherein: the water contact angle of the outer surface of each of the porous hollow fiber membranes is 90° or greater, a hydrophobic polymer is adhered to at least some of the locations among the non-adhesively anchored locations of the porous hollow fiber membranes,
and wherein the locations from one end to the other end in the lengthwise direction among the non-adhesively anchored locations are represented as 0% to 100% on both the inner surface and outer surface of each porous hollow fiber membrane, either or both the amount of hydrophobic polymer per membrane area adhering to locations at 0 to 5% from the one end and the amount of hydrophobic polymer per membrane area adhering to locations at 95 to 100% from the one end are greater than the amount of hydrophobic polymer per membrane area present in locations at 40 to 60% from the one end wherein a raw water introduction unit is disposed in so that the non-adhesively anchored location of each porous hollow fiber membrane is nearest to the raw water introduction unit at a location within less than 50% from the one end, and the amount of the hydrophobic polymer per membrane area of the porous hollow fiber membrane satisfies the following relationship: [Amount of hydrophobic polymer at locations at 0 to 20% from the one end]>[a mount of hydrophobic polymer at locations at 95 to 100% from the one end]>[a mount of hydrophobic polymer at locations at 40 to 60% from the one end.
2. A module for membrane distillation comprising a housing, and a plurality of porous hollow fiber membranes each having both ends adhesively anchored to the housing, wherein: a hydrophobic polymer is adhered to at least some of the locations among the non-adhesively anchored locations of the porous hollow fiber membranes,
and wherein the locations from one end to the other end in the lengthwise direction among the non-adhesively anchored locations are represented as 0% to 100% on both the inner surface and outer surface of each porous hollow fiber membrane, both the amount of hydrophobic polymer per membrane area adhering to locations at 0 to 5% from the one end and the amount of hydrophobic polymer per membrane area adhering to locations at 95 to 100% from the one end are greater than the amount of hydrophobic polymer per membrane area present in locations at 40 to 60% from the one end
wherein a raw water introduction unit is disposed so that the non-adhesively anchored location of each porous hollow fiber membrane is nearest to the raw water introduction unit at a location within less than 50% from the one end, and the amount of the hydrophobic polymer per membrane area of the porous hollow fiber membrane satisfies the following relationship: [Amount of hydrophobic polymer at locations at 0 to 20% from the one end]>[a mount of hydrophobic polymer at locations at 95 to 100% from the one end]>[a mount of hydrophobic polymer at locations at 40 to 60% from the one end].
3. The module for membrane distillation according to claim 1 , wherein at locations at 0 to 20% from the one end, the amount of hydrophobic polymer per membrane area on the raw water entering surface of the porous hollow fiber membrane is greater than the amount of hydrophobic polymer per membrane area on the vapor exiting surface of the porous hollow fiber membrane.
4. A membrane distillation device for water production,
comprising a module for membrane distillation according to claim 1 .
5. The membrane distillation device according to claim 4 , wherein: the membrane distillation device further comprises a cooling device connected with the module for membrane distillation, the module for membrane distillation is constructed so that each of the porous hollow fiber membranes is anchored in the vertical direction with the one end directed downward, and raw water is introduced into the porous hollow fiber membranes from the one end, and the lower end of the connecting member between the module for membrane distillation and the cooling device is at a position higher than ½ of the total height of the non-adhesively anchored locations of the porous hollow fiber membranes.
6. The membrane distillation device according to claim 4 , wherein: the module for membrane distillation is constructed so that each of the porous hollow fiber membranes is anchored in the vertical direction with the one end directed downward, and raw water is introduced into the porous hollow fiber membranes from the one end, and the module for membrane distillation has a discharge port at a position in the vertical direction corresponding to a position lower than ½ of the total height of the non-adhesively anchored locations of the porous hollow fiber membranes.
7. The module for membrane distillation according to claim 2 , wherein at locations at 0 to 20% from the one end, the amount of hydrophobic polymer per membrane area on the raw water entering surface of the porous hollow fiber membrane is greater than the amount of hydrophobic polymer per membrane area on the vapor exiting surface of the porous hollow fiber membrane.
8. The module for membrane distillation according to claim 1 , wherein at locations at 0 to 20% from the one end, the amount of hydrophobic polymer per membrane area on the raw water entering surface of the porous hollow fiber membrane is greater than the amount of hydrophobic polymer per membrane area on the vapor exiting surface of the porous hollow fiber membrane.
9. A membrane distillation device for water production,
comprising a module for membrane distillation according to claim 2 .
10. A membrane distillation device for water production, comprising a module for membrane distillation according to claim 1 .
11. A membrane distillation device for water production,
comprising a module for membrane distillation according to claim 3 .
12. The membrane distillation device according to claim 5 , wherein: the module for membrane distillation is constructed so that each of the porous hollow fiber membranes is anchored in the vertical direction with the one end directed downward, and raw water is introduced into the porous hollow fiber membranes from the one end, and the module for membrane distillation has a discharge port at a position in the vertical direction corresponding to a position lower than ½ of the total height of the non-adhesively anchored locations of the porous hollow fiber membranes.