Regeneration method of titanium silicalite molecular sieve catalyst
A titanium-silicon molecular sieve and catalyst technology, which is applied in the field of titanium-silicon molecular sieve catalyst regeneration, can solve problems such as an effective regeneration method for a titanium-silicon molecular sieve Ti-MWW catalyst, etc., and achieve the effects of simple and easy operation and easy process control.
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Embodiment 1
[0027] The deactivated Ti-MWW molecular sieves come from deactivated catalysts run in the ammoximation reaction of butanone.
[0028] In the first step, the Ti-MWW molecular sieve of deactivation: the weight ratio=1:30 of acidic compound solution, the concentration of acidic compound solution is 0.5mol / l, and acidic compound is nitric acid; In the second step, the first step makes The reaction mixture was reacted at 100°C for 2 hours; in the third step, the Ti-MWW molecular sieve treated with acid: the weight ratio=1:10 of the basic compound solution, wherein the concentration of the basic compound solution was 3mol / l, and the basic The compound is piperidine; in the fourth step, the reaction mixture obtained in the third step is hydrothermally treated at 170° C. for 24 hours under its own pressure to obtain an alkali-treated Ti-MWW molecular sieve, which is then filtered, washed, dried and roasted to obtain Regenerated Ti-MWW molecular sieves.
Embodiment 2
[0030] Implementation process is except following difference, and all the other are all the same with embodiment 1:
[0031] In the first step, the Ti-MWW molecular sieve of inactivation: the weight ratio=1:50 of acidic compound solution, the concentration of acidic compound solution is 0.1mol / l, and acidic compound is sulfuric acid; In the second step, the first step makes The reaction mixture was reacted at 80°C for 1 hour; in the third step, the acid-treated Ti-MWW molecular sieve: the weight ratio of the basic compound solution=1:20, wherein the concentration of the basic compound solution was 0.5mol / l; Among the four steps, the reaction mixture obtained in the third step is hydrothermally treated at 120° C. under its own pressure. A regenerated Ti-MWW molecular sieve was obtained.
Embodiment 3
[0033] Implementation process is except following difference, and all the other are all the same with embodiment 1:
[0034] In the first step, the Ti-MWW molecular sieve of deactivation: the weight ratio=1:10 of acidic compound solution, the concentration of acidic compound solution is 2.0mol / l, and acidic compound is hydrochloric acid; In the second step, the first step makes The reaction mixture was reacted at 35°C for 8 hours; in the third step, the acid-treated Ti-MWW molecular sieve: the weight ratio of the basic compound solution=1:5, wherein the concentration of the basic compound solution was 5mol / l; the fourth In the first step, the reaction mixture prepared in the third step was hydrothermally treated at 180°C for 12 hours under its own pressure. A regenerated Ti-MWW molecular sieve was obtained.
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