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

Active Publication Date: 2011-03-30
CHINA PETROLEUM & CHEM CORP +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For example, in the liquid-phase hydrogenation reaction system disclosed in CN200680018017.3, the pressure and liquid level in the reactor are further controlled by controlling the amount of mixed hydrogen in the liquid-phase feed. The liquid level or pressure changes constantly, and the amount of supplemented hydrogen may be less than the amount of hydrogen required for the reaction. For example, when there are more small molecule hydrocarbons produced under abnormal conditions, the liquid level in the reactor will drop. At this time, the control system The best adjustment method is to reduce the amount of mixed hydrogen in the liquid phase raw material. If it is reduced too much, the amount of hydrogen may not be enough to maintain the normal hydrogenation reaction, which will have an adverse effect on the stability of the reaction.

Method used

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  • Method and reaction system for liquid phase cycling hydrotreatment
  • Method and reaction system for liquid phase cycling hydrotreatment

Examples

Experimental program
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Effect test

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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Abstract

The invention discloses a method and a reaction system for liquid phase cycling hydrotreatment. In the method, part of a liquid phase product after the hydrotreatment is mixed with fresh raw oil in a cycling mode to form a liquid phase material; hydrogen is mixed into the liquid phase material; the hydrogen mixed amount is 1 to 20 times that of the dissolved hydrogen which makes the reaction system saturated under a reaction condition; the liquid phase material mixed and dissolved with the hydrogen is put into a reactor; a hydrogenation catalyst bed is arranged in the reactor and is immersed in the liquid phase material; the upper part of the reactor is provided with a gas phase space; a pressure control system communicated with the gas phase space is arranged on the reactor and controls the pressure in the reactor by controlling the gas exhaust quantity; and the liquid phase material dissolved with the hydrogen is put into the hydrogenation catalyst bed of the reactor to perform hydrogenation reaction. Compared with the prior art, the method ensures that the liquid phase cycling hydrotreatment can be controlled and operated stably, and obtain an ideal reaction effect.

Description

technical field [0001] The invention relates to a liquid-phase circulating hydrogenation treatment method and a reaction system, in particular to a liquid-phase hydrogenation treatment method and a reaction system by increasing dissolved hydrogen through liquid-phase product circulation. Background technique [0002] Reducing the content of sulfur and aromatics in diesel can reduce the emission of solid particles in the exhaust of diesel vehicles and reduce air pollution. my country's light diesel oil specifications and standards will soon be implemented with reference to the Euro III standard, which requires the sulfur to be less than 350 μg / g, and the Euro IV standard, which requires the sulfur to be less than 50 μg / g. In order to cope with the production of diesel oil with new emission standards, on the one hand, it is necessary to solve key technical problems, build a hydrogenation unit to carry out deep hydrodesulfurization of diesel oil, increase the cetane number, and...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G49/00C10G49/26C10G65/02C10G65/04C10G65/12
Inventor 方向晨叶杏园朱华兴李扬李立权王月霞刘继华张光黎牛世坤薛浩师敬伟曾茜胡敏赵予川
Owner CHINA PETROLEUM & CHEM CORP
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