Catalyst for removing olefins in reformate and preparation method of catalyst
A technology for removing olefins and catalysts, applied in the field of catalysts for removing trace olefins and its preparation, can solve problems such as increased energy consumption and loss of aromatics, and achieve the effects of improving utilization, reducing dealkylation, and reducing dosage
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Embodiment 1
[0020] ① 51 parts by weight of commercially available MCM-22 molecular sieve, 1 part by weight of alumina dry rubber powder, FeCl 3 30 parts by weight were added to the mixer and mixed for 5 minutes. Add dilute nitric acid with a concentration of 1wt%, mix, knead, extrude into a cylindrical shape with a diameter of ∮1.5×2mm, dry at 120°C for 2 hours, and collect the product;
[0021] ②Add the product of step ① into the aqueous solution of scandium nitrate, stand and impregnate at 35°C for 10 hours to make the catalyst contain 0.1 parts by weight of scandium nitrate, and roast at 600°C for 4 hours, the obtained product number is KC-1. Example 2
Embodiment 2
[0022] The molecular sieve adopts 25 parts by weight of β-type molecular sieve and 26 parts by weight of Y-type molecular sieve, and the Lewis acid adopts ZnCl 2 1 part by weight, using water to mix, knead and extrude molecular sieves, Lewis acid and alumina dry rubber powder; the catalyst contains 1.5 parts by weight of cerium nitrate; roasting at 300 ° C for 10 hours; other is the same as in Example 1, the product obtained The number is KC-2.
Embodiment 3
[0024] The molecular sieve adopts 30 parts by weight of X-type molecular sieve and 35 parts by weight of ZSM-5 type molecular sieve, and the Lewis acid adopts AlF 3 40 parts by weight; the catalyst contains 3 parts by weight of cerium nitrate; roasting at 800° C. for 1 hour, and the others are the same as in Example 1, and the obtained product number is KC-3.
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