Catalytic conversion method for producing high-octane petrol from crude oil
A technology of high-octane gasoline and catalytic conversion method, applied in catalytic cracking, cracking, petroleum industry and other directions, can solve the problems of poor gasoline properties, affecting gasoline octane number, and high energy consumption
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Embodiment 1
[0079] This example follows figure 1 The process of the test is carried out, and the raw material oil A is directly used as the raw material oil for catalytic cracking, and the test is carried out on the medium-sized device of the riser reactor, and the raw material oil A enters the reaction zone I. Reaction temperature 505°C, weight hourly space velocity 30h -1, the weight ratio of catalyst to raw oil is 10, and the weight ratio of water vapor to raw oil is 0.15 to carry out the cracking reaction; the reaction product oil gas and the catalyst to be born with charcoal are separated in the settler, and the product is carried out in the separation system according to the distillation range Cutting, so as to obtain products such as propylene, gasoline, diesel oil and catalytic wax oil (fraction greater than 330 ° C). The operating conditions and product distribution are listed in Table 2.
[0080] As can be seen from Table 2, the gasoline yield is as high as 43.28% by weight, i...
Embodiment 2
[0082] This example follows the attached image 3 The test is carried out according to the process, the raw material oil A is directly used as the easily cracked raw material oil of catalytic cracking, and the test is carried out on a medium-sized device with a riser reactor. The easy-cracked raw material oil enters the middle and upper part of the reaction zone I, and the difficult-to-cracked raw material oil enters the reaction zone I. bottom. 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...
Embodiment 3
[0085] This embodiment is the same as the test device of Example 2. The raw material oil B is 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 raw oil enters the bottom of reaction zone I. At the bottom of the reaction zone I, the refractory raw material oil is heated at a reaction temperature of 620°C and a weight hourly space velocity of 180h -1 , the weight ratio of catalytic cracking catalyst to refractory feed oil is 90, and the weight ratio of water vapor to refractory feed oil is 0.20 to carry out the cracking reaction; Hourly space velocity 60h -1 The cracking reaction is carried out under the condition that the weight ratio of catalytic cracking catalyst to easily cracked raw oil is 10, and the weight ratio of water vapor to easily cracked raw oil is 0.15; in addition, the supplementary part of the raw catalyst that has been stripped from the stripping section enters ...
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