Method for synthesizing NaA zeolite membrane on macroporous carrier
A zeolite molecular sieve membrane, macroporous carrier technology, applied in chemical instruments and methods, membrane, membrane technology and other directions, can solve the application field limitation, difficult to obtain high flux and selectivity, chemical stability, thermal stability mechanical problems such as poor stability, to achieve the effect of high repeatability, excellent separation performance, and suitable for large-scale applications
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[0022] Example 1
[0023] Step 1. Carrier tube pretreatment
[0024] The surface of the carrier tube was sanded with 600# and 800# waterproof sandpaper in turn until the surface of the carrier was smooth, and then ultrasonically vibrated with acid and alkali to remove residues in the carrier pores, washed with deionized water to neutrality, and dried naturally. Finally, it is dried at 150°C for use.
[0025] Step 2. Preparation of carrier seed layer
[0026] (1) Using hot dipping-wiping method to coat large seed crystals on the processed carrier tube: Raise the self-made NaA molecular sieve with a grain size of 1~3μm to 550℃ at a rate of 1K / min, and keep it 4h to remove the organic template in the molecular sieve, and then configure it into a 10% seed solution, and quickly immerse the carrier tube that has been baked at 180°C for 4h into the above seed solution. The immersion time is 20s. Afterwards, the carrier tube coated with the seed crystals is dried in an oven at 50-100°C, and...
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[0031] Example 2
[0032] Step 1. Carrier tube pretreatment
[0033] Same as step 1 in Example 1.
[0034] Step 2. Preparation of carrier seed layer
[0035] This time, only the hot dip-wiping method was used to coat the large seed crystals on the surface of the carrier, and the small seed crystals were not coated. The procedure is the same as the procedure (1) in step 2 in embodiment 1.
[0036] Step 3. Preparation of NaA zeolite molecular sieve membrane
[0037] Since only large seed crystals are applied, the separation selectivity of the NaA zeolite membrane synthesized by one-step crystallization needs to be improved. In order to further improve the separation performance of the NaA zeolite membrane, a two-step crystallization synthesis is adopted. The first step of the synthesis process is completely the same as step 3 in Example 1. In the second step of synthesis, the conditions and formula are changed. The specific implementation process is as follows: Put 6.80g NaAlO in a 200m...
Example Embodiment
[0039] Example 3
[0040] The membrane tubes synthesized in Example 1 and Example 2 were studied on the pervaporation performance of ethanol / water system respectively, and the process is as follows image 3 As shown, for an ethanol / water system with an ethanol mass fraction of 90%, the operating temperature is 70°C, and the vacuum degree on the permeate side is 200-400 Pa. The separation coefficient and permeation flux of the NaA molecular sieve membrane synthesized are respectively 5000- 10000 and 1.5~2.0kg / m 2 h. It exhibits good separation performance and has important industrial application value and practical significance.
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