Industrial sulfur tolerant catalyst for vapor ethylation of coking benzene to prepare ethyl benzene
A catalyst, ethylation technology, applied in physical/chemical process catalysts, molecular sieve catalysts, catalyst activation/preparation, etc., can solve problems such as difficulty in meeting long-term stable operation
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Embodiment 1
[0015] Nano NaZSM-5 (silicon aluminum molar ratio SiO 2 / Al 2 o 3 is 30) and α-Al 2 o 3 ·H 2 O is mixed at a ratio of 70:30, adding 2 to 3% of the dry basis of scallop powder and 10wt% of concentrated nitric acid aqueous solution, kneaded, extruded into strips, dried at 110°C, and roasted at 540°C for 3 hours to make sodium ZSM- 5 zeolite molecular sieves; use 0.4mol / L NH 4 NO 3 Exchange three times, wash with deionized water between each two times, dry at 110°C, bake at 540°C for six hours; finally soak in 0.6 mol / L nitric acid aqueous solution for 24 hours, wash with deionized water to pH ≈ 7, and dry at 110°C , Calcined at 540° C. for 3 hours to obtain a nano-hydrogen ZSM-5 catalyst with a diameter of 1.5 mm.
[0016] The above catalyst is treated with water steam for 2 hours at 500°C, and the weight space velocity is 0.5h -1 , and then impregnated with 0.06 mol / L lanthanum nitrate aqueous solution at room temperature for 4 hours, the weight ratio of lanthanum nitra...
Embodiment 2
[0025] The difference with Example 1 is that it is treated with high-temperature ammonia water vapor, and its treatment condition is 500 ° C, with 0.5 mol / liter of ammonia water vapor for 2 hours, and the weight space velocity is 0.5h -1 , all the other are identical with embodiment 1.
[0026] The conversion rate of coked benzene decreased from 57.2% to 24.0% after the catalyst was operated for 11 hours, the total selectivity of ethylbenzene increased from 85.6% to 96.0%, and the deactivation rate of the catalyst was 3.0% / hour.
Embodiment 3
[0028] The difference from Example 1 is that the water vapor treatment temperature is different, the specific process: under the condition of 400 ° C, water vapor treatment for 2 hours, the weight space velocity is 0.5h -1 , all the other are identical with embodiment 1.
[0029] The conversion rate of coked benzene dropped from 53.6% to 31.7% after the catalyst was operated for 25 hours, the total selectivity of ethylbenzene rose from 81.5% to 94.1%, and the deactivation rate of the catalyst was 0.88 percentage points / hour.
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