Catalytic cracking method for producing low-carbon olefins and light aromatic hydrocarbons
A technology for catalytic cracking and low-carbon olefins, applied in chemical instruments and methods, multi-stage series-connected refining and cracking process treatment, hydrocarbons, etc. efficiency, high BTX yield, and the effect of improving economic and social benefits
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preparation example Construction
[0059] The present invention also provides a method for preparing the catalytic cracking catalyst, comprising preparing the phosphorus-containing and metal-loaded IMF structure molecular sieve, and combining the obtained phosphorus-containing and metal-loaded IMF structure molecular sieve with Y-type molecular sieve, natural minerals , the precursor sol of oxide is mixed and beaten, and spray-dried; wherein the preparation method of phosphorus-containing and metal-loaded IMF structure molecular sieves comprises:
[0060] a. Desiliconizing the sodium-type IMF structure molecular sieve in an alkaline solution to obtain a desiliconization molecular sieve; b. performing an ammonium exchange treatment on the desilication molecular sieve obtained in step a to obtain an ammonium exchange molecular sieve; The total dry basis weight of the ammonium-exchanged molecular sieve is a benchmark, and the sodium content of the ammonium-exchanged molecular sieve is less than 0.2 weight %; dealu...
Embodiment approach
[0071] According to one embodiment of the present invention, when the method of the present invention is carried out in riser reactor, generally carry out as follows:
[0072]The regenerated catalyst (catalyst for catalytic cracking) enters the pre-lift section of the riser reactor and flows upward under the action of the pre-lift medium. The preheated raw oil and atomized steam are injected into the lower part of the riser reactor to contact the regenerated catalyst. The catalytic cracking reaction flows upward at the same time; the reacted oil and gas and the catalyst to be produced enter the fluidized bed reactor through the outlet of the riser reactor, and the reacted oil and gas react again, and the reacted stream enters the cyclone separator through the outlet of the riser reactor, and the separated reaction The oil and gas extraction device is further separated to obtain fractions such as methane, ethylene, propylene, C4 hydrocarbons, and pyrolysis gasoline rich in light...
Embodiment 1
[0107] according to figure 1 The flow process of the test is carried out, the raw oil is a vacuum distillate oil, and the catalyst A of the present invention is used to test on a medium-sized device, operated at normal pressure, and the preheated raw oil enters the bottom of the riser, at a reaction temperature of 565 ° C and a reaction time of 2.0 seconds , the weight ratio of catalytic cracking catalyst and raw oil is 10, and the cracking reaction is carried out under the condition that the weight ratio of water vapor and raw oil is 0.25, and the reaction oil gas and steam and the catalyst to be born enter the fluidized bed reactor from the reactor outlet, and Reaction temperature 540°C, weight hourly space velocity 3.4h -1 The reaction continues under the condition of seconds, and the post-reaction stream enters the closed cyclone, and the reaction oil gas and the unborn catalyst are quickly separated, and the reaction oil gas is cut according to the distillation range in t...
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