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Modified porous membrane material, preparation method, and liquid membrane separation method of carbon dioxide

A carbon dioxide, inorganic porous material technology, applied in separation methods, semi-permeable membrane separation, dispersed particle separation and other directions, can solve problems such as liquid loss of supporting liquid membrane membrane, achieve the effect of avoiding loss and improving convenience of use

Active Publication Date: 2019-12-31
NANJING TECH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] The purpose of the present invention is to solve the problem of the loss of the supporting liquid membrane membrane liquid, and at the same time retain the high carbon dioxide effect of the ionic liquid, and propose a membrane material amination modification method for enhancing the separation of carbon dioxide by the water supporting liquid membrane

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  • Modified porous membrane material, preparation method, and liquid membrane separation method of carbon dioxide
  • Modified porous membrane material, preparation method, and liquid membrane separation method of carbon dioxide
  • Modified porous membrane material, preparation method, and liquid membrane separation method of carbon dioxide

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preparation example Construction

[0043] The preparation method of the above-mentioned modified porous membrane material comprises the following steps:

[0044] The silane coupling agent containing amine groups is dissolved in an organic solvent as a modifier; the porous membrane material is immersed in the modifier for grafting reaction. After the reaction is completed, it is cleaned and dried to obtain a modified porous membrane material.

[0045] In one embodiment, the silane coupling agent containing amine groups: selected from, for example, N, N-dimethyl-3-aminopropyltrimethoxysilane, (3-aminopropyl)trimethoxysilane, etc. Wait.

[0046] In one embodiment, the organic solvent contains at least one of ethanol, acetone, dimethylacetamide (DMAC), and tetrahydrofuran (THF).

[0047] In one embodiment, the reaction conditions are that the temperature is 20-40° C., and the reaction time is 1-24 h.

Embodiment 1

[0049]Wash the inner membrane of the tubular ceramic membrane with an average pore diameter of 100 nm (geometric dimensions: the effective length of the membrane is 8cm, the outer diameter is 12cm, the inner diameter is 8cm, and the porosity is about 40%) and put it in a drying oven to dry for 1 to 2 hours , the silane coupling agent (N,N-dimethyl-3-aminopropyltrimethoxysilane (DMAPS)) containing amine groups was added dropwise into absolute ethanol to prepare 15 mmol / L modified In the modified solution, the porous membrane material was immersed in the modified solution, and reacted in a constant temperature water bath at a temperature of 35°C for 12 hours. After the full reaction was completed, it was washed and dried to obtain a membrane material with tertiary amine groups on the surface. The surface infrared spectrum of the modified membrane material is as follows: figure 1 shown. (N,N-Dimethyl-3-aminopropyl)trimethoxysilane (DMAPS) has the following structure:

[0050] ...

Embodiment 2

[0055] Wash the inner membrane of the tubular ceramic membrane with an average pore diameter of 200nm (geometric dimensions: the effective length of the membrane is 8cm, the outer diameter is 12cm, the inner diameter is 8cm, and the porosity is about 40%) and put it in a drying oven to dry for 1-2 hours. Add the silane coupling agent containing amine groups ((3-aminopropyl)trimethoxysilane) dropwise into acetone and dissolve to prepare a 50 mmol / L modification solution, and immerse the porous membrane material in the modification solution In the process, the reaction was carried out in a constant temperature water bath at a temperature of 30°C for 24 hours, and after the full reaction was completed, it was washed and dried to obtain a membrane material with tertiary amine groups on the surface. The membrane material is used in the gas absorption of the gas-liquid membrane contactor, and water is used as the absorbent, and it is found that the mass transfer flux of carbon dioxid...

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Abstract

The invention relates to a membrane modification method for enhancing liquid membrane separation of carbon dioxide. The membrane modification method comprises the following steps: grafting an organicmatter containing amine groups on a membrane material, and loading water in pores and channels of a porous membrane to prepare a supporting liquid membrane for mixed gas separation experiment of carbon dioxide. According to the membrane modification method, amine groups are introduced through chemical grafting reaction, so that water has certain alkalinity when serving as a membrane solution, compared with an alkaline solution serving as the membrane solution, loss of effective alkaline substances can be avoided, and meanwhile, the permeation flux of carbon dioxide is also improved.

Description

technical field [0001] The invention belongs to the modification of membrane materials, in particular to the amination modification of a membrane material supporting a liquid membrane and its application in enhancing the separation of carbon dioxide. Background technique [0002] In recent years, the greenhouse effect has been one of the most concerned environmental issues, and the main source of the greenhouse effect is CO 2 , which are mainly emitted by power plants, steel plants and chemical plants. From the perspective of preventing global warming, the development of efficient capture and recovery technology for carbon dioxide has become a top priority. In addition to CH 4 The extraction of natural gas as the main component also contains CO 2 , need to recover and remove CO from natural gas 2 , to prevent CO 2 Corrosion of gas pipelines during gas transportation. In addition, there are many CO 2 and need to remove CO 2 system to be processed. [0003] Currentl...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D71/82B01D53/22B01D67/00B01D69/02B01D71/02C01B32/50
CPCB01D71/82B01D71/024B01D69/02B01D67/0079B01D53/228C01B32/50B01D2256/22Y02C20/40Y02P20/151Y02A50/20B01D2257/102B01D2257/7025B01D2257/104B01D2257/108B01D2257/502B01D67/00931B01D71/027B01D71/70C04B38/00C04B2111/00801C04B35/10C04B35/14C04B35/46C04B35/48C04B38/0054C04B38/0074B01D2323/21834B01D2325/02834B01D2325/02833B01D53/1475B01D53/1493B01D53/229B01D69/04B01D69/06B01D2252/103B01D2257/504B01D2323/08
Inventor 范益群徐鹏邱鸣慧符开云陈献富孔祥力龚大为
Owner NANJING TECH UNIV