Method for modifying molecular sieve
A molecular sieve and modification technology, applied in the direction of octahedral crystalline aluminum silicate zeolite, crystalline aluminosilicate zeolite, etc.
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Embodiment 1
[0031] The modification process adopted in this embodiment is: resin primary exchange→roasting→resin secondary exchange→roasting→product. The specific operation process is as follows:
[0032] First, weigh 1000g of dry NaY particles, and configure it into a NaY slurry with a total volume of 7L in the beating container T-1. The amount of resin in the resin column 3 is 2400ml. After the slurry is separated in the ceramic membrane, the obtained clear water enters the resin column. , the thick slurry enters the beating container, and the effluent from the resin column also enters the beating container, and reacts at an exchange temperature of 30°C for 60 minutes, and the pH value of the effluent from the resin column is 5.4. Next, the NaY slurry was taken out and filtered by suction, and the obtained primary exchange product was roasted at 600°C. After the roasting was completed, it was placed in T-1 again, and the resin was used for secondary exchange. After the first exchange, f...
Embodiment 2
[0034] The modification process adopted in this embodiment is: resin → first exchange → roasting → ammonium salt secondary → exchange roasting → product, and its specific operation process is as follows:
[0035] First, take 1000g of dry NaY particles, and configure it into a NaY slurry with a total volume of 7L in a beating container. The amount of resin in the resin column 3 is 2400ml. After the slurry is separated in the ceramic membrane, the obtained clear water enters the resin column and thickens the slurry. Enter the beating container, the resin column effluent also enters the beating container, the two react at an exchange temperature of 20°C for 10min, the pH value of the resin column effluent is 5.3, then take out the NaY slurry and filter it, and the obtained primary exchange product is roasted at 500°C for 1h After the roasting is completed, it is beaten with 3000ml deionized water to form a slurry, and the ammonium salt is used for direct contact with the secondary...
Embodiment 3
[0037] The modification process adopted in this embodiment is: primary ammonium salt exchange→roasting→resin secondary exchange→roasting→product, and its specific operation process is as follows:
[0038] First, weigh 1000g of dry NaY particles, make a slurry with 3000ml of deionized water, and conduct a direct contact exchange with ammonium salt. The amount of ammonium salt is 350g, the exchange temperature is 95°C, and the exchange time is 60min. Then, the product obtained from one exchange is suction-filtered and roasted at 650°C for 1.5h. After roasting, the NaY molecular sieve is configured into a NaY slurry with a total volume of 7L in the beating container 1. The resin volume in the resin column 3 is 3600ml. Separation, clear water 6 enters the resin column 3, the thick stock 5 enters the beating container 1, and the resin column effluent 7 also enters the beating container 1. The two react at an exchange temperature of 50 ° C for 30 minutes. The pH value of the resin co...
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Abstract
Description
Claims
Application Information
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