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High-throughput carbon dioxide separation cellulose ether derivative composite membrane and preparation method thereof

A technology of cellulose ethers and carbon dioxide, applied in separation methods, chemical instruments and methods, educts, etc., can solve the problems of process limitations, cortical defects, and low separation selectivity, and achieve good pressure resistance and fast permeability , the effect of a wide range of sources

Active Publication Date: 2016-08-17
DALIAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In 1994, Liu Guixiang and others used non-woven fabric as the support layer to prepare an asymmetric membrane of ethyl cellulose by phase inversion method for the separation of oxygen and nitrogen. However, due to the limitation of the process, the cortex was defective and the separation selectivity was low.

Method used

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  • High-throughput carbon dioxide separation cellulose ether derivative composite membrane and preparation method thereof
  • High-throughput carbon dioxide separation cellulose ether derivative composite membrane and preparation method thereof
  • High-throughput carbon dioxide separation cellulose ether derivative composite membrane and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0049] Solution preparation: accurately weigh 92g ethanol (analytical pure) and 8g methylcellulose powder (analytical pure, average degree of substitution 1.85, average degree of polymerization 2000) by electronic balance; Mix in the bottle, seal the bottle mouth, and dissolve with magnetic stirring at 40°C for 24 hours to form a homogeneous solution; use a 100-mesh filter cloth to filter the solution, and then stand at room temperature (the temperature of the film-making room is controlled at 25°C) for 24 hours to defoam. That is, 8wt.% methylcellulose / ethanol coating solution is obtained, which is ready for use.

[0050] Porous support layer pretreatment: self-made polyacrylonitrile asymmetric porous support layer (surface porosity about 68%, average pore diameter about 73nm) was dried in a constant temperature drying oven (50°C) for 8h, cooled to room temperature 25°C; The supporting layer is fixed on the flat plate and placed horizontally for use.

[0051] Scrape coating ...

Embodiment 2

[0059]Solution preparation: accurately weigh 96g ethyl acetate (analytical pure) and 4g hydroxypropyl cellulose powder (analytical pure, average degree of substitution 1.70, average degree of polymerization 1500) by electronic balance; ethyl acetate and hydroxypropyl cellulose Mix in a ground-mouth Erlenmeyer flask, seal the bottle mouth, and dissolve with magnetic stirring at 60°C for 12 hours to form a homogeneous solution; use a 100-mesh filter cloth to filter the solution, and then statically Set aside for 24 hours for defoaming to obtain a 4wt.% hydroxypropyl cellulose / ethyl acetate coating solution for use.

[0060] Porous support layer pretreatment: The purchased polypropylene asymmetric porous support layer (surface porosity about 78%, average pore diameter about 185nm) is soaked in acetone to remove oily pollutants, transferred to deionized water to remove acetone and other hydrophilic substances, After natural air drying, dry in a constant temperature drying oven (50...

Embodiment 3

[0069] Solution preparation: accurately weigh 88g of tetrahydrofuran (analytical grade) and 12g of ethyl cellulose powder (analytical grade, average degree of substitution 2.25, average degree of polymerization 1200) by electronic balance; Mix in medium, seal the bottle mouth, and dissolve with magnetic stirring at 30°C for 24 hours to form a homogeneous solution; use a 100-mesh filter cloth to filter the solution, and then stand at room temperature (the temperature of the film-making room is controlled at 25°C) for 24 hours to defoam, that is A 12wt.% ethylcellulose / tetrahydrofuran coating solution was obtained for use.

[0070] Porous support layer pretreatment: homemade polyvinylidene fluoride asymmetric porous support layer (surface porosity about 60%, average pore diameter about 25nm) was dried in a constant temperature drying oven (50°C) for 8h, cooled to room temperature 25°C; A good support layer is fixed on a flat plate and placed horizontally for use.

[0071] Scrap...

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Abstract

The invention relates to a high-flux carbon dioxide separation cellulose ethers derivative composite membrane and a preparation method thereof, which belong to the field of gas separation. The surface of a polymer porous supporting membrane is coated with a cellulose ethers derivative coating solution to form the composite membrane with a cellulose ethers derivative selective compacting layer of 2 to 20 micrometers. The preparation method comprises the steps of mixing a cellulose ethers derivative with a good solvent, stirring and defoaming at the temperature of 25 to 80 DEG C, removing solid impurities, and preparing the cellulose ethers derivative coating solution in the content of 2 to 12 percent by weight; and coating the surface of the polymer porous supporting membrane with the cellulose ethers derivative coating solution, removing the solvent, and drying and curing the cellulose ethers derivative coating solution to form the cellulose ethers derivative selective compacting layer. The high-flux carbon dioxide separation cellulose ethers derivative composite membrane has high CO2 selectivity and high permeability and is better than a traditional CO2 separation membrane; moreover, the stability of the composite membrane is higher than that of an existing promoter transferring membrane; the raw material is easily available, the price is low, and no toxicity and no pollution exist.

Description

technical field [0001] The invention relates to a method for separating carbon dioxide (CO2) from industrial gases based on a selective permeation mechanism. 2 ) high-performance cellulose ether derivative composite membrane, and a preparation method of the membrane, which belong to the field of gas separation. This gas separation composite membrane utilizes the affinity of the ether oxygen bond functional groups in cellulose ether derivatives to preferentially pass through CO 2 , and prepare an ultra-thin defect-free cellulose ether derivative selective dense layer on the surface of the polymer porous support membrane by the method of the present invention, and realize CO 2 Osmotic high flux and high selectivity. Background technique [0002] Removing carbon dioxide from gases is a ubiquitous separation process in fields such as petroleum, chemical, energy and environment. CO in natural gas and manufactured gas 2 It will reduce the calorific value of the fuel, and the f...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D69/12B01D71/12B01D67/00B01D53/22C01B31/20C01B32/50
CPCY02C20/40Y02P20/151
Inventor 阮雪华贺高红姚从春代岩焉晓明李保军
Owner DALIAN UNIV OF TECH