Regeneration method for composite material containing beta molecular sieve in alkylation reaction
A technology of alkylation reaction and β molecular sieve, which is applied in molecular sieve catalysts, chemical instruments and methods, chemical/physical processes, etc., can solve the problems of complex regeneration process and high energy consumption, and achieve effective regeneration effect
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Embodiment 1
[0035] Put 5.0 grams of the raw agent B1', 5.0 g of tetrahydrofuran and 5.0 g of ethanol into the tank reactor together. After the temperature is stabilized at 40 ° C and the pressure reaches 1 Mpa, start stirring, and take out the catalyst after cooling down for 1 hour. , filtered, and dried to obtain a regenerant, which is denoted as B1'-1, wherein the particle size of the nano-β molecular sieve remains unchanged.
[0036] The acid strength analysis results of B1′-1 are shown in Table 1.
[0037] Add B1'-12.0 grams in the fixed-bed reactor, when the reactor was heated up to 80°C and the pressure reached 2MPa, the raw material of 100g isobutane and 1-butene was added at a space velocity of 2.0g / g.h (isobutane: 1-butene=10:1) was reacted, and after 100 minutes, the product was collected and detected. The reaction results are shown in Table 1.
Embodiment 2
[0039] Same as Example 1, except that the eluent is 10.0 g tetrahydrofuran, and the temperature is stabilized at 70° C. to obtain a regenerant, which is denoted as B1′-2, wherein the particle size of the nano-β molecular sieve remains unchanged.
[0040] The acid strength analysis results of B1'-2 and the reaction results of the regenerant in the fixed-bed reactor (reaction conditions and catalyst consumption are the same as in Example 1) are shown in Table 1.
Embodiment 3
[0042] The same as Example 1, the difference is that the eluent is 5.0g tetrahydrofuran and 10.0g dichloroethane to obtain a regenerant, which is denoted as B1'-3, wherein the particle size of the nano-beta molecular sieve remains unchanged.
[0043] The acid strength analysis results of B1'-3 and the reaction results of the regenerant in the fixed-bed reactor (reaction conditions and catalyst consumption are the same as in Example 1) are shown in Table 1.
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