Two zeolite-containing catalyst for ethene and benzene alkylation, and preparation method and application thereof
A technology for benzene alkylation and catalyst, which is applied to the catalyst for preparing ethylbenzene by the alkylation reaction of low-concentration ethylene and benzene and the field of preparation thereof, and can solve the problem of high xylene impurity content, high alkylation reaction temperature and high reaction temperature problem, to achieve the effect of reducing carbon deposition reaction, low reaction temperature and high activity
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Embodiment 1
[0029] The preparation process of the catalyst E-1 of the present invention is as follows:
[0030] (1) Configure 0.5mol / L phosphoric acid aqueous solution, and then adopt equal volume immersion method with BETA (SiO 2 / Al 2 O 3 The molar ratio is 28) and ZSM-5 (SiO 2 / Al 2 O 3 The molar ratio is 75). The two hydrogen molecular sieves are evenly mixed (the mass ratio is 8:1). After being immersed at 80°C for 2 hours, they are dried at 120°C and roasted in air at 550°C for 5 hours to obtain BETA and ZSM-5 modifications. The molecular sieve is denoted as S-1, and the weight content of phosphorus in the zeolite is 1.5%.
[0031] (2) Mix the modified molecular sieve S-1 and alumina powder obtained in step (1) on a dry basis of 60:40, and then add 100ml of water and 2.5ml of concentrated nitric acid (with a mass concentration of 66.5%). Kneading to make it into a paste-like plastic, extruding a cylindrical bar with a diameter of 1.5mm on an extruder, drying the cylindrical bar at 100°C ...
Embodiment 2
[0034] Preparation of catalyst E-2 of the present invention
[0035] (1) Configure 0.5mol / L ammonium dihydrogen phosphate aqueous solution, and then use equal volume immersion method with BETA (SiO 2 / Al 2 O 3 The molar ratio is 28) and ZSM-5 (SiO 2 / Al 2 O 3 The molar ratio is 75) The two hydrogen molecular sieves are evenly mixed (the mass ratio is 5:1). After immersing at 80°C for 2 hours, they are dried at 120°C and roasted in air at 550°C for 5 hours to obtain BETA and ZSM-5 modified The molecular sieve is denoted as S-2, and the weight content of phosphorus in the zeolite is 2.5%.
[0036] (2) Mix the modified molecular sieve S-2 and alumina powder obtained in step (1) on a dry basis of 20:80, and then add 100ml of water and 2.5ml of concentrated nitric acid (the mass concentration is 66.5%), fully Kneading to make it into a paste-like plastic, extrude a cylindrical strip with a diameter of 1.5mm on an extruder, dry the cylindrical strip at 100°C for 16 hours, and then calcin...
Embodiment 3
[0039] Preparation of catalyst E-3 of the present invention
[0040] The preparation process of the catalyst E-3 of the present invention is the same as that of Example 1, except that the ethanol solution of triethyl phosphate is used instead of the aqueous phosphoric acid solution. The evaluation results of the prepared catalyst E-3 of the present invention are shown in Table 2.
[0041] (1) Configure a 1.0mol / L ethyl phosphate ethanol solution, and then use an equal volume immersion method with BETA (SiO 2 / Al 2 O 3 The molar ratio is 58) and ZSM-5 (SiO 2 / Al 2 O 3 The molar ratio is 105) The two hydrogen molecular sieves are evenly mixed (the mass ratio is 8:1). After immersing at 80°C for 2 hours, they are dried at 120°C and roasted in air at 550°C for 5 hours to obtain BETA and ZSM-5 modifications. The molecular sieve is denoted as S-3, and the weight content of phosphorus in the zeolite is 5.0%.
[0042] (2) Mix the modified molecular sieve S-3 and alumina powder obtained in st...
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