Method for preparing light-weight fuel oil and propylene from inferior raw oil
A technology for low-quality feedstock oil and light fuel oil, which is applied in the fields of petroleum industry, cracking, organic chemistry, etc. It can solve the problems of increased yield of dry gas and coke, and achieve the effect of increasing the operation cycle and improving the properties of feedstock oil
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Embodiment 1
[0057] This example follows figure 1 The process of vacuum residue oil A is used as the raw material for catalytic cracking, and the test is carried out on the medium-sized device of the riser reactor. The inferior raw material enters the bottom of the reaction zone I, contacts and reacts with the catalyst GZ-1, and in the reaction zone At the bottom of I, poor-quality raw materials are processed at a reaction temperature of 600°C and a weight hourly space velocity of 100h -1, the weight ratio of catalyst to raw material is 6, and the weight ratio of water vapor to raw material is 0.05, and the cracking reaction is carried out; in reaction zone II, oil gas is mixed with circulating propane, C4 hydrocarbons and diesel oil at a reaction temperature of 500 ° C and a weight hourly space velocity 30h -1 The cracking reaction is carried out under the condition that the weight ratio of water vapor to raw material is 0.05, the oil gas and the catalyst to be charred are separated in t...
Embodiment 2
[0063] This example follows figure 2 Inferior hydrogenation residue raw material C is used as the raw material for catalytic cracking, and the test is carried out on the medium-sized device of the riser reactor. The inferior raw material enters the bottom of the reaction zone I, contacts with the catalyst GZ-1 and reacts. At the bottom of zone I, inferior raw materials are reacted at a reaction temperature of 600°C and a weight hourly space velocity of 100h -1 , the weight ratio of catalyst to raw material is 6, and the weight ratio of water vapor to raw material is 0.05, and the cracking reaction is carried out; 30h -1 The cracking reaction is carried out under the condition that the weight ratio of water vapor to raw material is 0.05, the oil gas and the catalyst to be charred are separated in the settler, and the products are cut according to the distillation range in the separation system, so as to obtain dry gas, liquefied gas, propylene, gasoline, diesel oil And catal...
Embodiment 3
[0069] This example is based on figure 2 The high-acid crude oil raw material E is used as the raw material for catalytic cracking, and the test is carried out on the medium-sized device of the riser reactor. The inferior raw material enters the bottom of the reaction zone I, contacts and reacts with the catalyst GZ-1, and in the reaction zone I Bottom, low-quality raw materials at a reaction temperature of 600°C and a weight hourly space velocity of 100h -1 , the weight ratio of catalyst to raw material is 6, and the weight ratio of water vapor to raw material is 0.05, and the cracking reaction is carried out; in reaction zone II, oil and gas are heated at a reaction temperature of 500°C and a weight hourly space velocity of 30h -1 The cracking reaction is carried out under the condition that the weight ratio of water vapor to raw material is 0.05, the oil gas and the catalyst to be charred are separated in the settler, and the products are cut according to the distillation ...
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