Method for preparing high-quality fuel oil from inferior crude oil
A technology for inferior raw material oil and raw material oil, which is applied in the field of catalytic conversion of hydrocarbon oil, can solve the problems of low cetane number of diesel oil, reduced dry gas yield and coke yield, etc. The effect of improved properties and improved operating cycle
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Embodiment 1
[0059] This embodiment is carried out according to the accompanying drawings. The vacuum residue raw material 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 lower part of the reaction zone I, contacts with the catalyst GZ-1 and generates Reaction, in the lower part of the reaction zone I, the inferior raw material is at a reaction temperature of 595°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 with carbon are separated in the settle...
Embodiment 2
[0065] This embodiment is to carry out test according to the flow process of accompanying drawing, high-acid crude oil raw material B is used as the raw material of catalytic cracking, is tested on the medium-sized device of riser reactor, and inferior raw material enters reaction zone I lower part, contacts with catalyst GZ-1 and The reaction occurs, and in the lower part of the reaction zone I, the inferior raw materials are heated at a reaction temperature of 595°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 with carbon are separated in the settler, a...
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