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A kind of heavy oil hydrogenation reactor and hydrogenation method

A heavy oil hydrogenation and reactor technology, which is applied in chemical instruments and methods, hydrogenation process, hydrocarbon oil treatment, etc., can solve the problems of high viscosity of heavy oil, long residence time, coking of catalyst, etc.

Active Publication Date: 2021-10-08
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the following problems still exist in the heavy oil liquid-phase hydrogenation hydrogenation reactor and the reaction process: (1) The heavy oil has a high viscosity and the hydrogen oil mass transfer rate is low, resulting in a low reaction rate; (2) The reaction residence time in the heavy oil hydrogenation process Difficult to control, short residence time cannot reach the required depth of reaction, and long reaction residence time, side reactions or cracking and serious problems of catalyst coking
[0008] In summary, most of the heavy oil hydrogenation reactors and upflow liquid phase hydrogenation reactors in the prior art are based on improving the process through existing equipment, adopting new hydrogen dissolution equipment or multiple hydrogen dissolution, etc. method to improve the hydrogenation reaction efficiency, but did not solve the problems of low reaction rate, insufficient conversion depth, uneven temperature rise in the heavy oil liquid phase hydrogenation reaction process, and low liquid yield, side reactions and cracking reactions caused by long residence time. serious problem

Method used

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  • A kind of heavy oil hydrogenation reactor and hydrogenation method
  • A kind of heavy oil hydrogenation reactor and hydrogenation method
  • A kind of heavy oil hydrogenation reactor and hydrogenation method

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Effect test

Embodiment 1

[0042] Attached figure 1 In the method described, the catalyst I used in the inner cylinder I of the heavy oil hydrogenation reactor adopts the FZC protective agent / 3996 catalyst developed by the Fushun Petrochemical Research Institute, and the catalyst II in the annular space adopts the FZC protective agent developed by the Fushun Petrochemical Research Institute / / For the 3936 catalyst, the FZC protective agent in the inner cylinder I is 14% of the total catalyst volume of the inner cylinder, and the FZC protective agent in the annular space is 14% of the total catalyst volume in the annular space. The hydrogen contained in the feed to the heavy oil hydrogenation reactor is 5.30% of the mass of the feedstock oil (the sum of fresh feedstock oil and circulating oil); The sum of oil) is 6.28% of the mass; the circulation ratio is 2.5.

[0043] The reaction conditions of the inner cylinder I of the hydrogenation reactor are as follows: the reaction temperature is 380-393°C, the...

Embodiment 2

[0047] Attached figure 1In the described method, the catalyst I used in the hydrogenation reactor inner cylinder I adopts the FZC protective agent / FF-26 catalyst developed by Fushun Petrochemical Research Institute, and the catalyst II in the annular space adopts the FZC protective agent / FF-26 developed by Fushun Petrochemical Research Institute. 3996 catalyst, wherein the FZC protective agent in the inner cylinder I is 15% of the total catalyst volume of the inner cylinder, and the FZC protective agent in the annular space is 15% of the total catalyst volume in the annular space. The hydrogen contained in the hydrogenation reactor feed is 6.62% of the mass of the raw material oil (the sum of fresh raw material oil and circulating oil); sum) 5.20% of the mass.

[0048] The reaction conditions of the inner cylinder I of the hydrogenation reactor are as follows: the reaction temperature is 380-393°C, the reaction pressure is 15.0MPaG, and the liquid hourly volume space velocity...

Embodiment 3

[0052] Attached figure 1 In the method described, the catalyst I used in the hydrogenation reactor inner cylinder I adopts the FZC protective agent / FF-46 catalyst developed by the Fushun Petrochemical Research Institute, and the catalyst II in the annular space adopts the FZC protective agent / FF-46 developed by the Fushun Petrochemical Research Institute. FF-26 catalyst, wherein the FZC protective agent is 15% of the total catalyst volume. The hydrogen contained in the hydrogenation reactor feed is 4.20% of the mass of the raw material oil (the sum of fresh raw material oil and circulating oil); sum) 8.15% of the mass.

[0053] The reaction conditions of the inner cylinder I of the hydrogenation reactor are as follows: the reaction temperature is 378-390°C, the reaction pressure is 15.0MPaG, and the liquid hourly volume space velocity is 1.0h -1 ;The reaction conditions in the annular space are as follows: the reaction temperature is 391-410°C, the reaction pressure is 14.5M...

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Abstract

The invention discloses a heavy oil hydrogenation reactor and a hydrogenation method. The reactor consists of an outer cylinder of the reactor, an inner cylinder I and an inner cylinder II arranged along the axial direction of the reactor. The cross-sectional area of ​​the inner cylinder I gradually decreases from top to bottom, and the cross-sectional area of ​​the inner cylinder II gradually decreases from top to bottom. increase; an annular space is formed between the inner cylinder I, the inner cylinder II and the outer cylinder of the reactor; the inner cylinder I is filled with a hydrogenation catalyst I, and the annular space is filled with a hydrogenation catalyst II, and the activity of the hydrogenation catalyst I is higher than Activity of Hydrogenation Catalyst II. The present invention reduces the viscosity of the material through the viscosity-reducing component installed in the inner cylinder II, and then passes through the inner cylinder I and the annular space to undergo a hydrogenation reaction, improves the driving force and reaction rate of the mass transfer process of the heavy oil liquid phase hydrogenation reaction, and controls the reaction between the reaction material and the hydrogenation reaction. The contact time of different active catalysts can slow down the coking of the catalyst surface, reduce the deep cracking reaction of light oil, and improve the liquid yield and heavy impurity removal conversion rate of heavy oil liquid phase hydrogenation reaction process.

Description

technical field [0001] The invention belongs to the field of petrochemical industry, and in particular relates to a heavy oil hydrogenation reactor and a hydrogenation method. Background technique [0002] With the hydrogenation of crude oil becoming heavier and inferior, the composition of crude oil is getting heavier, that is, the proportion of heavy crude oil is getting higher and higher. Therefore, the progress of heavy oil hydroprocessing technology has become a key point in the research of hydrogenation process. one. Heavy oil hydrogenation reactors are divided into various types, such as fixed bed hydrogenation reactors, suspension bed hydrogenation reactors, ebullating bed hydrogenation reactors, etc. Fixed bed hydrogenation reactors are the most widely used. The bed reactor can handle various types of heavy oil products, and has shown unique advantages in the process of oil hydrogenation, such as low-quality oil residues and coal liquefied oils, which are prone to ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/04C10G67/00
CPCB01J8/04B01J8/0492B01J8/0496C10G67/00B01J2208/025C10G2300/4006C10G2300/4012C10G2300/4018C10G65/02B01J8/44B01J2208/0061B01J8/22B01J8/34B01J2208/00911B01J2208/00884C10G45/02C10G49/00B01J8/065C10G2300/1077C10G2300/202C10G2300/205C10G2300/206C10G2300/301C10G2300/302C10G2300/308
Inventor 杨秀娜周峰阮宗琳何佳
Owner CHINA PETROLEUM & CHEM CORP
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