Ammonium ion exchange method of molecular sieve
A technology of ammonium ion exchange and ion exchange, which is applied in the field of ammonium ion exchange of molecular sieves, can solve the problems of ammonium ion exchange and achieve high efficiency and low water consumption
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example 1
[0036] This example illustrates the method provided by the invention.
[0037] With 30 grams of calcined rare earth hydrogen Y molecular sieve (rare earth oxide content is 2.0% by weight, wherein, La 2 o 3 Content is 1.7 wt%, CeO 2 The content is 0.2% by weight, the content of other rare earth metal oxides is 0.1% by weight, the content of sodium oxide is 4.6% by weight, and the unit cell constant is 24.63 angstroms, produced by Lanzhou Refining and Chemical Company Catalyst Factory), deionized water and sodium hydroxide (chemical Pure) beating together, so that the content of molecular sieve in the obtained slurry is 200 grams per liter, the amount of sodium hydroxide is 1% by weight of molecular sieve, heated to 80 °C under stirring, and the obtained slurry is poured into the filter of a Buchner funnel On the cloth, vacuumize the filter bottle to 0.03 MPa, and filter under this vacuum until there is no liquid on the surface of the filter cake, and record the linear velocit...
example 2
[0042] This example illustrates the method provided by the invention.
[0043] By the method of example 1, a calcined rare-earth hydrogen Y molecular sieve is beaten, filtered, exchanged, washed and recorded separation filtration speed, exchange filtration speed and washing filtration speed, the difference is to replace sodium hydroxide with 25% by weight of strong ammonia water, The consumption of concentrated ammonia water makes the consumption of ammonia be 3 weight % of molecular sieve consumption. The results are listed in Tables 1 and 2, respectively.
example 3
[0045] This example illustrates the method provided by the invention.
[0046] By the method of example 1, a calcined rare earth hydrogen Y molecular sieve is beaten, filtered, exchanged, washed and record separation and filtration speed, exchange filtration speed and washing filtration speed, the difference is that the rare earth oxidation rare earth content of the rare earth hydrogen Y molecular sieve used is 7.0 wt. % where La 2 o 3 Content is 2.3 wt%, CeO 2 The content is 4.1% by weight, the content of other rare earth oxides is 0.6% by weight, the content of sodium oxide is 4.0% by weight, and the content of molecular sieve in the slurry is 150 g / L. The results are listed in Tables 1 and 2, respectively.
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