C8 Aromatics Isomerization-Separation Coupling Reaction Method
A technology for isomerization and coupling reaction of aromatic hydrocarbons, which is applied in the field of isomerization of alkyl aromatic hydrocarbons, and can solve problems such as xylene loss
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[0036] The preparation method of the phosphorus-modified hydrogen-type molecular sieve of the invention comprises: impregnating the hydrogen-type molecular sieve with a phosphorus-containing compound solution dissolved in water. The impregnation pressure is preferably 0.1-1.0 MPa, the impregnation temperature is preferably 75-180°C, the liquid / solid volume ratio of the impregnation liquid to the molecular sieve is 0.7-3.0, and the impregnation time is preferably 5-24 hours. The solid obtained after impregnation is dried and calcined to obtain phosphorus-modified molecular sieves. The phosphorus-containing compound used for impregnation is selected from one or more of ammonium phosphate, diammonium hydrogen phosphate, ammonium dihydrogen phosphate, aluminum phosphate, phosphoric anhydride, phosphorous acid, ammonium phosphite and phosphoric acid.
[0037] In the above process of preparing phosphorus-modified molecular sieves, the drying temperature is 80-130°C, preferably 100-1...
example 1
[0050] Get 200 grams of silica / alumina mol ratio as 90, crystallinity is 85% HZSM-5 molecular sieve, 150 grams of silica / alumina mol ratio is 550, crystallinity is 76% NaZSM-5 and 50 grams of alumina Mix well, add nitric acid aqueous solution with a mass concentration of 4% by mass according to the ratio of solid / liquid mass ratio 3:1, extrude into strips, dry the strips at 120°C for 6 hours, pelletize, and roast at 550°C for 5 hours. Catalyst A-1 was prepared, which contained 50% by mass of HZSM-5 molecular sieve, 37.5% by mass of NaZSM-5 molecular sieve and 12.5% by mass of alumina.
example 2
[0052] Prepare catalyst by the method for example 1, difference is that 280 grams of HZSM-5 molecular sieves, 100 grams of NaZSM-5 molecular sieves and 20 grams of aluminum oxide are mixed, and catalyst A-2 is obtained through extruding, drying, roasting, wherein contains 70 mass % of HZSM-5 molecular sieve, 25% by mass of NaZSM-5 and 5% by mass of alumina.
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