A process and system for producing more gasoline and aromatics
A technology of aromatics and process, applied in the field of petroleum refining, can solve the problems of high hydrogen consumption, harsh operating conditions, and ineffective utilization of aromatic components, and achieve the effects of high yield, improved component properties, and significant economic benefits
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Embodiment 1
[0053] This embodiment provides a process system for producing more gasoline and aromatics, which includes: a heavy oil riser 2 , a first fractionation tower 4 , a hydrogenation reactor 9 , a second fractionation tower 11 and an aromatics extraction device 14 .
[0054] Wherein, the product outlet of the heavy oil riser 2 communicates with the inlet of the first fractionation tower 4;
[0055] The diesel fraction outlet of the first fractionation tower 4 communicates with the inlet of the hydrogenation reactor 9, and the outlet of the hydrogenation reactor 9 communicates with the second fractionation tower 11;
[0056] The heavy fraction 13 outlet of the second fractionation tower 11 communicates with the aromatics extraction unit 14; the raffinate 16 outlet of the aromatics extraction unit 14 and / or the light fraction 12 outlet of the second fractionation tower 11 It communicates with the entrance of the heavy oil riser 2.
Embodiment 2
[0058] combined with figure 1 , present embodiment provides a kind of technique of the technique of producing gasoline and aromatics, it comprises the following steps:
[0059] (1) catalytic cracking
[0060] The heavy oil raw material 1 enters the bottom of the heavy oil riser 2 for catalytic cracking. The reaction conditions of the heavy oil riser 2 are: riser outlet temperature 510°C, agent-oil ratio 6.5, reaction pressure 0.15MPa, and reaction time 3.1s , Atomized water vapor accounts for 3w% of the feed amount.
[0061] After the heavy oil catalytic cracking, the heavy oil catalytic cracking product 3 enters the first fractionation tower 4 for fractionation. The first gas 5, catalytic gasoline 6 and first oil slurry 8 are separated by the first separation tower to the downstream system, and the separated catalytic diesel oil 7 enters the fixed-bed hydrogenation reactor 9 for hydrofining.
[0062] The conditions for hydrofining are:
[0063] (2) Hydrofining
[0064] P...
Embodiment 3
[0075] This embodiment provides a process for producing more gasoline and aromatics, the difference lies in the different parameters, the difference is as follows: the outlet temperature of the heavy oil riser of the catalytic cracking unit is 500°C.
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