A kind of methyl halide preparation isobutylene catalyst with anti-carbon deposition performance and preparation method thereof
A halogenated methane and catalyst technology, applied in the field of halogenated methane to isobutene catalyst and its preparation, can solve the problems of low selectivity of single product, undiscovered methyl bromide and the like, achieve simple preparation method, easy industrialization and high product selectivity Effect
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Embodiment 1
[0027] Firstly, zinc nitrate was weighed and dissolved in deionized water, loaded on the alumina carrier by equal volume impregnation method, dried at 80°C for 6h, and calcined at 400°C for 6h to obtain ZnO / Al 2 o 3 ; Then take thorium nitrate and dissolve it in water, adopt equal volume impregnation method to load on ZnO / Al 2 o 3, dried at 120°C for 4h and calcined at 450°C for 6h to obtain ZnO-ThO 2 / Al 2 o 3 . Use a continuous flow fixed-bed reactor to treat the catalyst precursor under a mixed atmosphere, wherein the volume content of methyl bromide is 30%, and the balance is nitrogen, and the treatment conditions are 230°C, 0.1MPa, 100h -1 , the time is 4h. Prepared methyl halide to produce isobutylene catalyst, by weight, ZnBr 2 content of 10.4%, ZnO content of 1.2%, ThO 2 The content is 0.8%. The total acid content below 450°C in the catalyst is 0.82mmol / g, and the acid content between 250°C and 350°C accounts for 58.11% of the total acid content below 450°C. ...
Embodiment 2
[0030] Firstly, zinc nitrate was weighed and dissolved in deionized water, loaded on the alumina carrier by equal volume impregnation method, dried at 120°C for 4 hours, and calcined at 350°C for 8 hours to obtain ZnO / Al 2 o 3 ; Then take thorium nitrate and dissolve it in water, adopt equal volume impregnation method to load on ZnO / Al 2 o 3 , dried at 120°C for 4h and calcined at 400°C for 8h to obtain ZnO-ThO 2 / Al 2 o 3 . Use a continuous flow fixed-bed reactor to treat the catalyst precursor under a mixed atmosphere, wherein the volume content of methyl bromide is 30%, and the balance is nitrogen, and the treatment conditions are 230°C, 0.1MPa, 100h -1 , the time is 4h. Prepared methyl halide to produce isobutylene catalyst, by weight, ZnBr 2 content of 31.2%, ZnO content of 3.7%, ThO 2 The content is 0.8%. The total acid content below 450°C in the catalyst is 0.91mmol / g, and the acid content between 250°C and 350°C accounts for 50.19% of the total acid content be...
Embodiment 3
[0033] Firstly, zinc nitrate was weighed and dissolved in deionized water, loaded on the alumina carrier by equal volume impregnation method, dried at 100°C for 8h, and calcined at 400°C for 6h to obtain ZnO / Al 2 o 3 ; Then take thorium nitrate and dissolve it in water, adopt equal volume impregnation method to load on ZnO / Al 2 o 3 , dried at 120°C for 4h and calcined at 350°C for 8h to obtain ZnO-ThO 2 / Al 2 o 3 . Use a continuous flow fixed-bed reactor to treat the catalyst precursor under a mixed atmosphere, wherein the volume content of methyl bromide is 30%, and the balance is nitrogen, and the treatment conditions are 230°C, 0.1MPa, 100h -1 , the time is 4h. Prepared methyl halide to produce isobutylene catalyst, by weight, ZnBr 2 content of 41.9%, ZnO content of 6.2%, ThO 2 The content is 0.8%. The total acid content below 450°C in the catalyst is 0.71mmol / g, and the acid content at 250°C-350°C accounts for 62.72% of the total acid content below 450°C.
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