Catalyst for producing m-cresol through isomerization of o-cresol and preparation method of catalyst
A catalyst, o-cresol technology, applied in the field of molecular sieves, can solve the problems of high energy consumption, incapable of large-scale industrial production, complex catalyst recovery, etc.
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Embodiment 1
[0020] SiO of ZSM-5 molecular sieve raw powder 2 / Al 2 o 3 The molar ratio is 200, and the following modification method is adopted: the original powder of ZSM-5 molecular sieve is firstly treated with CaCl with a concentration of 0.1mol / L 2 Aqueous solution exchange modification, CaCl 2 The liquid-solid volume ratio of the aqueous solution to the ZSM-5 molecular sieve raw material is 5:1, and the treatment temperature is 80°C for 2 hours to obtain the Ca-ZSM-5 molecular sieve. Its XRD and SEM see figure 1 , figure 2 .
[0021] Mix Ca-ZSM-5 molecular sieve, silica sol, 1 wt% of the Ca-ZSM-5 molecular sieve and silica sol dry weight of scallop powder, knead, extrude, dry at 100°C for 5h, and roast at 550°C for 4h. Get a catalyst. Based on the catalyst weight, the content of Ca-ZSM-5 molecular sieve is 70%, and the rest is silicon oxide.
[0022] o-cresol isomerization to prepare m-cresol isomerization reaction, the raw material used is the toluene solution of o-cresol ...
Embodiment 2
[0026] SiO of ZSM-5 molecular sieve raw powder 2 / Al 2 o 3 The molar ratio is 400, and the following modification method is adopted: the original powder of ZSM-5 molecular sieve is firstly treated with CaCl with a concentration of 0.1mol / L 2 Aqueous solution exchange modification, CaCl 2 The liquid-solid volume ratio of the aqueous solution to the ZSM-5 molecular sieve raw material is 5:1, and the treatment temperature is 80°C for 2 hours to obtain the Ca-ZSM-5 molecular sieve. Its XRD and SEM see image 3 , Figure 4 .
[0027] Mix Ca-ZSM-5 molecular sieve, silica sol, 1 wt% of the Ca-ZSM-5 molecular sieve and silica sol dry weight of scallop powder, knead, extrude, dry at 100°C for 5h, and roast at 550°C for 4h. Get a catalyst. Based on the catalyst weight, the content of Ca-ZSM-5 molecular sieve is 70%, and the rest is silicon oxide.
[0028] The reaction evaluation was carried out according to the reaction conditions described in Example 1, and the reaction evaluat...
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