Low thermal conductivity hydrophilic-hydrophobic bipolar composite membrane as well as preparation method and application thereof

A composite membrane and low thermal conductivity technology, applied in chemical instruments and methods, membranes, membrane technology, etc., can solve the problems of immature technology, frosting on the cooler surface, high sensible heat transfer, etc., to reduce moisture diffusion resistance, high water The effect of steam permeation speed and simple preparation method

Inactive Publication Date: 2016-10-12
SOUTH CHINA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The cooling and dehumidification method needs to cool the temperature of the air below its dew point, and the cooled air needs to be heated before it can be sent into the room. During this process, the temperature and humidity cannot be controlled independently, resulting in low energy efficiency and high energy consumption; Moisture condenses on the surface of the cooler, making the cooler humid all the year round, providing a place for bacteria to grow and multiply, and seriously degrading the indoor air quality; and for conditions where the dew point temperature is too low, it is easy to cause frost on the cooler surface, which requires a special device Perform defrosting treatment on it. Membrane dehumidification is a passive dehumidification method, and its dehumidification capacity is controlled by the side with lower water vapor pressure in the wet exchange gas; membrane material is an important factor affecting membrane dehumidification. Good or bad determines the performance of the entire dehumidification process
Electrochemical dehumidification is a very novel dehumidification method, and its technology is not mature enough; moreover, a DC power supply is required in the dehumidification process, and the energy utilization is not high.
[0006] The disadvantage of existing membranes is that it is difficult to meet the contradiction between high moisture permeability and blocking the penetration of other gas molecules at the same time, and the thermal conductivity of the membrane material itself is too high, resulting in excessive sensible heat transfer and excessive energy loss.

Method used

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  • Low thermal conductivity hydrophilic-hydrophobic bipolar composite membrane as well as preparation method and application thereof
  • Low thermal conductivity hydrophilic-hydrophobic bipolar composite membrane as well as preparation method and application thereof
  • Low thermal conductivity hydrophilic-hydrophobic bipolar composite membrane as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0050] (1) Dissolve 7g of polyvinylidene fluoride and 1g of porogen in 100g of dimethyl sulfoxide and add 1g of hydrophobic silica aerogel, control the temperature to 60°C, and fully stir for 4 hours to dissolve , And let it stand for 12 hours to defoam, and use a wiper to control the wet thickness of the film at 100μm. After that, the coated glass plate was quickly thrown into the tap water bath. After 1 minute, the formed membrane was peeled off the glass plate, transferred to another water bath and allowed to stand for 24 hours to remove excess solvent, picked up and dried to obtain a porous membrane.

[0051] (2) 4g polyvinyl alcohol, 2g hydrophilic silica aerogel and 0.12g lithium chloride were stirred with 120g deionized water at 90°C for 1 hour to prepare a polyvinyl alcohol solution, and the above solution was allowed to stand still One day, the casting solution is formed; the above casting solution is poured on the 100 μm polyvinylidene fluoride porous film obtained in ...

Embodiment 2

[0054] (1) Dissolve 8g of polyvinylidene fluoride and 1g of porogen in 110g of dimethyl sulfoxide and add 2g of hydrophobic silica aerogel, control the temperature at 60°C, and fully stir for 4 hours to dissolve , And let it stand for 12 hours to defoam, and use a wiper to control the wet thickness of the film at 100μm. After that, the coated glass plate was quickly thrown into the tap water bath. After 1 minute, the formed membrane was peeled off the glass plate, transferred to another water bath and allowed to stand for 24 hours to remove excess solvent, picked up and dried to obtain a porous membrane.

[0055] (2) 2g polyvinyl alcohol, 1g hydrophilic silica aerogel and 0.10g lithium chloride were stirred with 120g deionized water at 90°C for 1 hour to prepare a polyvinyl alcohol solution, and the above solution was allowed to stand still One day, the casting solution is formed; the above casting solution is poured on the 100 μm polyvinylidene fluoride porous film obtained in ...

Embodiment 3

[0058] (1) Dissolve 9g of polyvinylidene fluoride and 2g of porogen in 100g of dimethyl sulfoxide and add 3g of hydrophobic silica aerogel, control the temperature to 60°C, and fully stir for 4 hours to dissolve , And let it stand for 12 hours to defoam. Use a wiper to control the wet thickness of the film to 70μm. After that, the coated glass plate was quickly thrown into the tap water bath. After 1 minute, the formed membrane was peeled off the glass plate, transferred to another water bath and allowed to stand for 24 hours to remove excess solvent, picked up and dried to obtain a porous membrane.

[0059] (2) 15g of polyvinyl alcohol, 5g of hydrophilic silica aerogel and 0.15g of lithium chloride were stirred with 150g of deionized water at 100°C for 2 hours to prepare a polyvinyl alcohol solution, and the above solution was allowed to stand still 3 days to form a casting solution; pour the casting solution onto the 70μm polyvinylidene fluoride porous membrane obtained in ste...

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Abstract

The invention belongs to the technical field of membrane separation materials and discloses a low thermal conductivity hydrophilic-hydrophobic bipolar composite membrane as well as a preparation method and application thereof. The composite membrane is composed of a porous supporting body layer with the thickness of 30-100mu m and an ultrathin skin layer with the thickness of 5-20mu m, wherein the porous supporting body layer is prepared from a hydrophobic polymer and hydrophobic silicon dioxide aerogel, and the ultrathin skin layer is prepared from a hydrophilic polymer and hydrophilic silicon dioxide aerogel. The preparation method of the composite membrane adopts a coating method, technology is simple, and equipment cost is low; and the obtained composite membrane has good permeability and gas selectivity, relatively low thermal conductivity and relatively high strength, can be widely applied to the fields of water treatment technology, air conditioning engineering, energy sources, chemical engineering, metallurgy, biochemical engineering and the like and is especially applicable to sea water desalination and independent air dehumidification.

Description

Technical field [0001] The invention belongs to the technical field of membrane separation materials, and specifically relates to a low thermal conductivity hydrophilic-hydrophobic bipolar composite membrane and a preparation method and application thereof. Background technique [0002] Freshwater resources are one of the most important material foundations for human survival and development. Seawater desalination and wastewater purification technologies are gradually becoming important means to solve the shortage of freshwater resources. [0003] Seawater desalination, also known as seawater desalination, is a process of separating salt and water in seawater. Commonly used seawater desalination methods include thermal method and membrane method. The thermal method mainly uses multi-stage flash evaporation, multi-effect distillation, and pressure steam distillation. The membrane method mainly refers to reverse osmosis. Thermal method usually consumes a large amount of high-grade...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D69/12B01D67/00B01D71/02B01D71/34
CPCB01D67/0079B01D69/12B01D71/027B01D71/34B01D2323/18B01D2325/24B01D2325/36B01D2325/38
Inventor 张立志李斯陶
Owner SOUTH CHINA UNIV OF TECH
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