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A kind of liquid phase hydrogenation reactor and hydrogenation method

A liquid-phase hydrogenation and reactor technology, which is applied in chemical instruments and methods, hydrotreating processes, hydrocarbon oil treatment, etc., can solve problems such as severe exotherm

Active Publication Date: 2022-07-08
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] Aiming at the deficiencies of the prior art, the present invention provides a liquid-phase hydrogenation reactor and a hydrogenation method, through the internal structure of the reactor, the material flow mode and the catalyst gradation method, the initial activity of the catalyst in the early stage of the hydrogenation reaction can be effectively controlled, and the reaction rate can be improved. The reaction conversion rate in the later stage solves the problem of severe heat release in the early stage of the reaction and the reaction product inhibits the reaction conversion rate in the later stage of the reaction, and at the same time achieves a higher hydrogenation reaction rate and reaction conversion rate in the early stage of the reaction and in the later stage of the reaction

Method used

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  • A kind of liquid phase hydrogenation reactor and hydrogenation method
  • A kind of liquid phase hydrogenation reactor and hydrogenation method
  • A kind of liquid phase hydrogenation reactor and hydrogenation method

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Effect test

Embodiment 1

[0042] with attached figure 1In the described method, the catalyst used in the conical inner cylinder of the hydrogenation reactor is FH-40C of Fushun Petrochemical Research Institute, the catalyst used in the annular cavity space is FHUDS-2; the hydrogen contained in the feed of the hydrogenation reactor is 0.23% (straight-run diesel feedstock) and 0.23% (catalyzed diesel feedstock) of the mass of feedstock oil (the sum of fresh feedstock oil and circulating oil), and the amount of hydrogen supplemented in the conical inner cylinder of the hydrogenation reactor is the feedstock oil (fresh feedstock oil and 0.25% (straight-run diesel feedstock) and 1.15% (catalyzed diesel feedstock) of the sum of circulating oil), and the hydrogen supply in the annular cavity is 0.13% ( straight-run diesel feedstock) and 0.62% (catalytic diesel feedstock). The reaction conditions of the conical inner cylinder of the hydrogenation reactor are as follows: the reaction temperature is 300-325 °C ...

Embodiment 2

[0045] with attached figure 1 In the described method, the catalyst used in the conical inner cylinder of the hydrogenation reactor is FH-40C of Fushun Petrochemical Research Institute, the catalyst used in the annular cavity is FHUDS-5, and the hydrogen contained in the feed of the hydrogenation reactor is 0.22% (straight-run diesel feedstock) and 0.25% (catalyzed diesel feedstock) of the mass of the feedstock oil (the sum of fresh feedstock oil and circulating oil), and the amount of hydrogen supplemented in the conical inner cylinder of the hydrogenation reactor is the feedstock oil (fresh feedstock oil and The sum of circulating oil) is 0.26% (straight-run diesel feedstock) and 1.08% (catalytic diesel feedstock), and the hydrogen supply in the annular cavity space is 0.12% by mass of the feedstock oil (sum of fresh feedstock oil and circulating oil). (straight-run diesel feedstock) and 0.65% (catalytic diesel feedstock). The reaction conditions of the conical inner cylind...

Embodiment 3

[0048] with attached figure 1 In the method, the catalyst used in the conical inner cylinder of the hydrogenation reactor is FHUDS-2 of Fushun Petrochemical Research Institute, the catalyst used in the annular cavity is FHUDS-5; the hydrogen contained in the feed of the hydrogenation reactor is the raw material 0.21% (straight-run diesel feedstock) and 0.23% (catalyzed diesel feedstock) of the oil (the sum of fresh feedstock oil and circulating oil), and the amount of hydrogen supplemented in the conical inner cylinder of the hydrogenation reactor is feedstock oil (fresh feedstock oil and circulating oil). 0.22% (straight-run diesel feedstock) and 1.14% (catalyst diesel feedstock) of the sum of oil), and the hydrogen supply in the annular cavity is 0.17% (straight-run diesel feedstock) of the mass of the feedstock oil (sum of fresh feedstock oil and circulating oil). Distillate diesel feedstock) and 0.58% (catalytic diesel feedstock). The reaction conditions of the conical in...

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Abstract

The invention discloses a liquid-phase hydrogenation reactor and a hydrogenation method. The liquid-phase hydrogenation reactor includes an inner cylinder and a reactor shell, the inner cylinder is conical, an annular cavity is formed between the inner cylinder and the reactor shell, and the cross-sectional area of ​​the annular cavity gradually increases from bottom to top; the top of the inner cylinder is The upper head is connected to the raw material inlet of the top of the reactor, and the bottom of the inner cylinder is communicated with the bottom of the annular cavity; the middle of the reactor is horizontally arranged with a ceramic membrane nano / micron component, and the ceramic membrane nano / micron component is connected to external hydrogen; the inner cylinder is filled with Hydrogenation catalyst I, the annular cavity is filled with hydrogenation catalyst II, the activity of hydrogenation catalyst I is lower than that of hydrogenation catalyst II; the flow mode of the material in the inner cylinder is from top to bottom; the flow mode of the material in the annular cavity For bottom up. The method of the invention can effectively control the initial activity of the liquid phase hydrogenation reaction and improve the conversion rate in the later stage of the reaction through the internal structure of the reactor, the material flow mode and the catalyst gradation.

Description

technical field [0001] The invention belongs to the field of petrochemical industry, in particular to a liquid-phase hydrogenation reactor and a hydrogenation method. Background technique [0002] Liquid-phase hydrogenation technology is a new type of hydrogenation technology. Hydrogen is dissolved in feedstock oil in advance, and the hydrogen required for hydrogenation is met by a large number of liquid-phase circulations, which overcomes the hydrogen diffusion in conventional trickle bed hydrogenation. Due to the influence of mass transfer, the hydrogenation reaction is carried out in the kinetic control zone. Therefore, compared with the traditional fixed-bed gas / liquid / solid three-phase hydrogenation process, the liquid-phase hydrogenation process has the advantages of fast hydrogenation reaction rate, high reaction High efficiency, low energy consumption, low investment and many other advantages have been widely recognized and applied. Liquid-phase hydrogenation reacto...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/04C10G67/00
CPCB01J8/04B01J8/0492B01J8/0496C10G67/00B01J2208/025C10G2300/4006C10G2300/4012C10G2300/4018Y02P20/52
Inventor 杨秀娜周峰何佳阮宗琳
Owner CHINA PETROLEUM & CHEM CORP
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