Preparation of SAPO-34 molecular sieve film for selectively separating methane gas

A SAPO-34, a technology for separating methane, applied in semi-permeable membrane separation, chemical instruments and methods, membrane technology and other directions, can solve the problems of no patent reports, reduce membrane permeability, increase paths, etc., to achieve good separation performance, repeatability Good performance and high repeatability

Inactive Publication Date: 2008-10-08
JILIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Stelter et al. reported that the method for secondary growth and synthesis of SAPO-34 membranes (Chinese Patent Application No. 97193836.9) was adsorbed on the carrier after modifying the charge on the surface of the seed crystal, but for carriers with large pore sizes, this method cannot synthesize continuous dense Noble et al. reported in-situ hydrothermal synthesis of SAPO-34 film on porous supports (Chinese Patent Application No. 200580008446.8), Min Enze et al. reported in-situ synthesis of SAPO on the surface of flat porous ceramics -34 film (Chinese Patent Application No. 96106353.X), but because the in-situ synthesis method is only applicable to carriers with less porosity (such as ceramic sheet, ceramic tub

Method used

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  • Preparation of SAPO-34 molecular sieve film for selectively separating methane gas
  • Preparation of SAPO-34 molecular sieve film for selectively separating methane gas
  • Preparation of SAPO-34 molecular sieve film for selectively separating methane gas

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0030] Example 1

[0031] Step A: Synthesis of SAPO-34 Molecular Sieve Seeds

[0032] Add 2 g of aluminum isopropoxide to 5 g of deionized water and stir well for hydrolysis. 1 g phosphoric acid solution (H 3 PO 4 , mass fraction 85%), 8.47 g tetraethylammonium hydroxide aqueous solution (TEAOH, mass fraction 20%), 0.32 g silica sol (SiO 2 Aqueous solution, mass fraction 30%), add 0.3 g of concentrated hydrochloric acid solution (HCl, mass fraction 37%), the pH value of the reaction mother liquor is 6 at this time, 180 ° C hydrothermal crystallization for 3 days, the product is taken out and washed with deionized water Drying to obtain seed crystal powder, the grain size of which is 3-5 microns.

[0033] Step B: Preparation of Seed Base Film

[0034] Add deionized water to the crystal seed powder obtained in step A, make a suspension of 3g / L, and use an ultrasonic cleaner (KQ-100DE type CNC ultrasonic Cleaner, Kunshan Ultrasonic Instrument Co., Ltd.) with deionized water...

Example Embodiment

[0037] Example 2

[0038] The difference from Example 1 is that after the synthesis, step C of Example 1 is repeated to synthesize the SAPO-34 molecular sieve membrane once again to repair the intercrystalline defects on the surface of the membrane. It can be seen from Table 1 that the separation performance of the membrane is further improved.

Example Embodiment

[0039] Example 3

[0040] The difference from Example 1 is that three samples are used in parallel tests according to this ratio to test the repeatability, and the rest are the same as those in Example 1. The results are listed in Table 2, and it can be seen that this method has good repeatability.

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Abstract

The invention relates to a novel method of SAPO-34 molecular sieve membrane for selectively separating methane gas by crystal guidance and secondary synthesis. The method includes three steps, namely synthesizing crystal seed, preparing basement membrane of crystal seed and synthesizing SAPO-34 molecular sieve membrane, in particular to the following steps: phosphoric acid, TEAOH and silica sol are added into adequately hydrolyzed aluminium isopropoxide to prepare a crystal seed solution of the molecular sieve and the molecular sieve composite mother solution; the crystal seed solution of the molecular sieve is prepared to be suspension after crystallization and rinsing for dripping onto a treated carrier; a basement membrane of crystal seed acquired is placed in a reaction kettle and is added with the molecular sieve composite mother solution for crystallization at a temperature ranging from 150 DEG C to 180 DEG C for 3 through 20 days, which is taken out for cleaning and drying and then is followed with actively removing a template agent at a temperature ranging from 400 DEG C to 600 DEG C. Synthesizing the molecular sieve membrane with the method of the invention is suitable for various porous supports with smooth surface, which is of high repetitiveness, good orientation, excellent separating property and ultrahigh gas permeability and is suitable for industrial application.

Description

technical field [0001] The invention belongs to the field of molecular sieve membrane preparation, and in particular relates to a preparation method of a SAPO-34 molecular sieve membrane for secondary synthesis and selective separation of methane gas induced by seed crystals. Background technique [0002] Membrane is an intermediate intervening phase that separates two phases of matter and makes them related to each other, and the process of mass and energy transmission occurs. Compared with well-known traditional separation methods, such as evaporation and fractionation, the membrane separation process has the outstanding advantages of high efficiency, low energy consumption, mild and simple operating conditions, and several other features, so it is widely used and developed rapidly. Separation membranes and corresponding membrane separation technologies have been widely used in food and beverage, medical and health, biotechnology, chemical metallurgy, environmental enginee...

Claims

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Application Information

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IPC IPC(8): B01D71/02
Inventor 朱广山裘式纶田宇阳
Owner JILIN UNIV
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