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A kind of hollow fiber inner wall naa molecular sieve pervaporation membrane dynamically synthesized in a continuous flow system and its synthesis method

A technology of pervaporation membrane and molecular sieve, applied in chemical instruments and methods, membrane technology, semi-permeable membrane separation, etc., can solve the problem that the synthetic liquid cannot be updated in time.

Active Publication Date: 2021-07-30
EAST CHINA UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In order to solve the limitation that the synthesis liquid cannot be updated in time due to the small space in the inner cavity of the small-diameter support, and to improve the technical problem of the effective length of the molecular sieve membrane tube, the present invention provides a dynamic synthesis of NaA molecular sieves on the inner wall of the hollow fiber in a continuous flow system Method of pervaporation membrane and NaA type molecular sieve pervaporation membrane on inner wall of hollow fiber

Method used

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  • A kind of hollow fiber inner wall naa molecular sieve pervaporation membrane dynamically synthesized in a continuous flow system and its synthesis method
  • A kind of hollow fiber inner wall naa molecular sieve pervaporation membrane dynamically synthesized in a continuous flow system and its synthesis method
  • A kind of hollow fiber inner wall naa molecular sieve pervaporation membrane dynamically synthesized in a continuous flow system and its synthesis method

Examples

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Effect test

Embodiment 1

[0029] Example 1: A method for dynamically synthesizing a hollow fiber inner wall NaA molecular sieve pervaporation membrane in a continuous flow system:

[0030] (1) α-Al with a length of 6cm 2 o 3 The hollow fiber is used as a support, soaked in 1.0mol / L sodium hydroxide solution for 10 hours, then ultrasonically cleaned with deionized water until neutral, and placed in an oven at 70°C to completely dry;

[0031] (2) ultrasonically dispersing NaA molecular sieve particles with a particle size between 90 and 150 nm in deionized water to prepare a seed crystal suspension with a solid content of 6 wt.%.

[0032] (3) Coating the seed layer: With the peristaltic pump as the driving force, the seed liquid prepared in step (2) was continuously passed through the inner cavity of the ceramic hollow fiber support at a flow rate of 3.0ml / min for 30s, and then reversed Flow and repeat this process. After the crystal coating is completed, place the support in a 60°C oven to dry for more ...

Embodiment 2

[0036] Example 2: A method for dynamically synthesizing a hollow fiber inner wall NaA molecular sieve pervaporation membrane in a continuous flow system:

[0037] Steps (1) to (4) are the same as in Example 1;

[0038] (5) Dynamic and continuous synthesis of NaA separation layer: seal the outer surface of the crystal-coated support and install it vertically in the synthesis device. The synthesis solution is always kept stirring at room temperature to maintain the uniformity of its components. At a flow rate of 0.26ml / min, it flows continuously through the pipeline of the device and the inner cavity of the support, and then returns to the main body of the synthetic liquid to form a circulation. The synthetic liquid is only preheated to 90°C in the pipeline before entering the support, and heated by a constant temperature. The device ensures that the temperature is always maintained after it enters the inner cavity of the support. After 6 hours of dynamic continuous reaction, th...

Embodiment 3

[0040] Example 3: A method for dynamically synthesizing a hollow fiber inner wall NaA molecular sieve pervaporation membrane in a continuous flow system:

[0041] Steps (1) to (4) are the same as in Example 1;

[0042] (5) Dynamic and continuous synthesis of NaA separation layer: seal the outer surface of the crystal-coated support and install it vertically in the synthesis device. The synthesis solution is always kept stirring at room temperature to maintain the uniformity of its components. At a flow rate of 0.52ml / min, it flows continuously through the pipeline of the device and the inner cavity of the support, and then returns to the main body of the synthetic liquid to form a circulation. The synthetic liquid is only preheated to 90°C in the pipeline before entering the support, and heated by a constant temperature. The device ensures that the temperature is always maintained after it enters the inner cavity of the support. After 6 hours of dynamic continuous reaction, th...

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Abstract

The invention discloses a method for dynamically synthesizing a NaA type molecular sieve pervaporation membrane on the inner wall of a hollow fiber in a continuous flow system and the prepared NaA type molecular sieve pervaporation membrane on the inner wall of a hollow fiber. seed suspension; coat the seed layer on the inner wall of the hollow fiber; prepare the synthetic solution; dynamically synthesize the molecular sieve membrane layer in the device for circulating the material and liquid, and finally obtain the NaA molecular sieve pervaporation membrane after post-processing. The invention has the advantages of high tolerance to the surface of the support body and the quality of the seed layer, excellent pervaporation separation performance of the membrane, good uniformity of the membrane layer and long effective length, and significant industrial practical application value.

Description

technical field [0001] The invention relates to the synthesis of molecular sieve membranes, in particular to a method for dynamically synthesizing a hollow fiber inner wall NaA molecular sieve pervaporation membrane in a continuous directional flow system and the synthesized hollow fiber inner wall NaA molecular sieve pervaporation membrane. Background technique [0002] Inorganic molecular sieve materials are widely used in the field of membrane separation because of their excellent physical and chemical properties. Compared with the separation membranes of other inorganic materials, the pore structure of the molecular sieve membrane is neat and uniform, and the pore size varies with the type of molecular sieve and is similar to the molecular size of many important industrial raw materials. In addition, its catalytic activity and good chemical and thermal stability Therefore, it has broad application prospects in many fields such as gas separation, pervaporation separation,...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D61/36B01D67/00B01D69/08B01D71/02
CPCB01D61/362B01D67/0039B01D69/08B01D71/028
Inventor 许振良曹悦李宇璇王明魏永明马晓华
Owner EAST CHINA UNIV OF SCI & TECH