Method and reaction system for liquid phase cycling hydrotreatment
A liquid-phase circulating hydrogenation and treatment method technology, which is applied in the direction of hydroprocessing process, hydrocarbon oil treatment, hydrocarbon oil treatment control/regulation, etc., can solve the problems of insufficient hydrogenation reaction, unfavorable reaction stability, and influence, and achieve reduction Cracking and other side reactions, reducing temperature rise, and ensuring stable supply
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Embodiment 1
[0058] according to figure 1 The operation process is to use ordinary second-line oil (sulfur content 2800μg / g) as raw material for hydrorefining and desulfurization, and the catalyst is the FH-UDS catalyst developed and produced by Fushun Petrochemical Research Institute. The theoretical dissolved hydrogen amount (0.18wt%) of the system for the determination of the reaction is tested first, and then the process of the method of the present invention is carried out. The reaction pressure is 6.4MPa, the reaction temperature is 360°C, and the volumetric space velocity of the reaction raw material oil is 6h -1 . The amount of hydrogen mixed in the fixed control oil is 0.19wt% (mixed hydrogen amount / feed amount, that is, the hydrogen mixed amount is 1.05 times of the saturated dissolved amount of the reaction state), and is a constant amount, and the circulation ratio (circulation oil volume: fresh raw material volume ) is 2:1, and the liquid volume and pressure in the reactor a...
Embodiment 2
[0062] according to figure 2 As shown in the process flow, two reactors are used in series. The mixed diesel feedstock was hydrotreated at 365°C for desulfurization and denitrogenation (sulfur content was 7500 μg / g, nitrogen content was 240 μg / g), and the catalyst was FHUDS-2 catalyst developed and produced by Fushun Petrochemical Research Institute. The amount of dissolved hydrogen in the reaction system (0.17wt%) is tested first, and then the process of the method of the present invention is carried out. The reaction pressure is 5.5MPa, and the volume space velocity of the reaction raw material oil is 3.2h -1 . The circulation ratio (circulation oil volume: fresh raw material volume) is 4: 1, and the amount of hydrogen mixed in the fixed control oil of each reactor is 0.72wt% (hydrogen mixed amount / feed amount, that is, the hydrogen mixed amount is the reaction 4.2 times of the state saturated solubility), and is a constant amount. As a result of the reaction, the sulfu...
Embodiment 3
[0064] according to Figure 4 As shown in the flow chart, the reactor is provided with two hydrogenation catalyst beds, and the catalyst volume ratio of the two catalyst beds is 1:1. Vacuum gas oil (VGO, with a nitrogen content of 2100 μg / g) was hydrotreated at 380 °C to remove nitrogen, and the catalyst was 3996 catalyst developed and produced by Fushun Petrochemical Research Institute. The amount of dissolved hydrogen (0.21wt%) in the reaction system is tested first, and then the process of the method of the present invention is carried out. The reaction pressure is 14.7MPa, and the volumetric space velocity of the reaction raw material oil is 1h -1 . The amount of hydrogen is 3 times the amount of dissolved hydrogen in the system, the circulation ratio of the first catalyst bed (circulation oil volume: fresh raw material volume) is 1: 1, and the circulation ratio of the second catalyst bed (total circulation oil volume: fresh raw material volume ) is 3: 1, that is, the a...
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