Catalyst conversion method for producing high-octane gasoline by using crude oil
A technology of high-octane gasoline and catalytic conversion method, which is applied in the direction of catalytic cracking, cracking, and petroleum industry, and can solve problems affecting gasoline octane number, poor gasoline properties, and insufficient utilization of gasoline latent content, etc.
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Embodiment 1
[0084] This example follows the attached image 3 MGCO-2 is used as the catalyst, and feedstock oil A is directly used as the easy-to-crack feedstock oil for catalytic cracking. The test is carried out on a medium-sized device with a riser reactor. The easy-to-crack feedstock oil enters the middle and upper part of the reaction zone I. Cracked raw oil enters the bottom of reaction zone I. At the bottom of reaction zone I, the refractory raw material oil is heated at a reaction temperature of 600°C and a weight hourly space velocity of 240h -1 , the weight ratio of catalytic cracking catalyst to refractory feed oil is 30, and the weight ratio of water vapor to refractory feed oil is 0.20 to carry out the cracking reaction; Hourly space velocity 90h -1 The cracking reaction is carried out under the condition that the weight ratio of the catalytic cracking catalyst to the easy-to-crack raw oil is 10, and the weight ratio of the water vapor to the easy-to-crack raw oil is 0.15. ...
Embodiment 2
[0090] This example follows the attached Figure 4 The test is carried out according to the process, with MGCO-2 as the catalyst, the raw material oil B is directly used as the difficult-to-crack raw material oil of catalytic cracking, and the test is carried out on a medium-sized device with a riser reactor. The cracked raw oil enters the upper part of the reaction zone I to react. At the bottom of the reaction zone I, the refractory feed oil is heated at a reaction temperature of 580°C and a weight hourly space velocity of 200h -1 , the weight ratio of catalytic cracking catalyst to refractory feed oil is 60, and the weight ratio of water vapor to refractory feed oil is 0.20 to carry out the cracking reaction; Hourly space velocity 120h -1 , the weight ratio of catalytic cracking catalyst to easily cracked raw oil is 30, and the weight ratio of water vapor to easily cracked raw oil is 0.15 to carry out the cracking reaction; in addition, the supplementary part of the raw c...
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