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A coal tar hydrotreating method and a coal tar processing method

A processing method and technology for hydrotreating pretreatment, applied in hydrotreating process, treating hydrocarbon oil, petroleum industry, etc., can solve the problems of difficult catalyst recovery, unstable operation process, harsh reaction conditions, etc., and achieve good hydrotreating effect, reduced ash content and water content, reduced tendency to green coke

Active Publication Date: 2017-11-24
HUNAN CHANGLING PETROCHEM SCI & TECH DEV CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the suspended bed hydrogenation process has the advantages of strong raw material adaptability, there are problems such as difficult catalyst recovery, unstable operation process, harsh reaction conditions, high investment and high safety risks.

Method used

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  • A coal tar hydrotreating method and a coal tar processing method
  • A coal tar hydrotreating method and a coal tar processing method
  • A coal tar hydrotreating method and a coal tar processing method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0114] (1) Pre-hydrogenation step

[0115] The structure of the gas-liquid mixer adopted in this embodiment is as follows: Figure 4 As shown, the components used to adjoin the liquid channel and the gas channel in the gas-liquid mixer are as follows image 3 The membrane tube shown (commercially purchased from Beijing Zhongtianyuan Environmental Engineering Co., Ltd.; the average pore diameter of the pores on the substrate is 100 μm; the average pore diameter of the pores on the porous membrane is 250 nm, and the pores on the porous membrane with a pore diameter in the range of 250-260 nm The proportion of the total pores is 95%; the porosity of the porous membrane is 45%); the porous membrane is located on the outer wall of the membrane tube; there are 19 channels evenly distributed, and the inner diameter of each liquid channel is 8mm. The channel on the membrane tube is used as a liquid channel, and the space formed by the outer wall of the membrane tube and the inner wal...

Embodiment 2

[0128] Adopt the method identical with embodiment 1 to process coal tar, difference is:

[0129] (1) Coal tar is a high-temperature coal tar extracted from fine chemicals such as phenol, naphthalene and anthracene, and its properties are shown in Table 1;

[0130] (2) In step (1), the components used to adjoin the liquid channel and the gas channel in the gas-liquid mixer are as follows figure 2 The membrane tube shown (commercially purchased from Beijing Zhongtianyuan Environmental Engineering Co., Ltd.; the average pore diameter of the pores on the substrate is 60 μm; the average pore diameter of the pores on the porous membrane is 50 nm, and the pores on the porous membrane with a pore diameter in the range of 20-200 nm The proportion of the total pores is 95%; the porosity of the porous membrane is 35%); the porous membrane is located on the inner wall of the membrane tube; there are 19 channels evenly distributed, and the inner diameter of each liquid channel is 3.3mm; t...

Embodiment 3

[0134] Adopt the method identical with embodiment 1 to process coal tar, difference is:

[0135] (1) Coal tar is a medium-low temperature coal tar by-product of dry distillation of semi-coke process, and its quality is listed in Table 1;

[0136] (2) In step (1), the member used to adjoin the liquid channel and the gas channel in the gas-liquid mixer is a pipe (commercially purchased from Beijing Zhongtianyuan Environmental Engineering Co., Ltd.; the average diameter of the holes on the pipe wall is 500nm , where the proportion of pores with a pore diameter in the range of 500-550nm to the total pores is 95%; the porosity is 25%); there are 19 channels evenly distributed, and the inner diameter of each liquid channel is 3.3mm. The filling rate of the pipe in the shell is 45%;

[0137] (3) In step (2), the fraction of the oil produced by hydrofining of coal tar with a distillate temperature greater than 150°C is used as the extractant, and the pre-hydrogenated oil is extracted...

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Abstract

The invention discloses a coal tar processing method. The method comprises: sending hydrogen gas into extracted or unextracted coal tar through pores with an average pore diameter of nanometer size to obtain hydrogen-containing coal tar; The tar is sent into the tubular reactor in the way of upward flow, and is contacted with the hydrogenation catalyst packed in the tubular reactor under the condition of liquid phase hydroprocessing to obtain the pre-hydrogenated oil; the pre-hydrogenated oil With or without extraction, hydrofinishing and optional hydrocracking. The method can effectively reduce the ash content and water content of coal tar, and provide qualified raw materials for subsequent hydrotreating. The method can also effectively reduce the coking tendency of the catalyst, prolong the service life of the hydrofining catalyst and the stable operation time of the hydrofining unit, and realize the treatment of the whole fraction of coal tar by using the fixed bed hydrogenation unit.

Description

technical field [0001] The invention relates to a coal tar hydrogenation treatment method, and the invention also relates to a coal tar processing method. Background technique [0002] The market price of coal tar is relatively low, and using petroleum hydrogenation technology to make it into clean fuel oil will have significant economic and social benefits. In recent years, my country's coal chemical technology has developed rapidly, and coal tar hydrogenation and upgrading to produce clean fuel technology has become an indispensable part of coal clean and efficient comprehensive utilization projects. [0003] Coal tar hydrogenation technology mainly has the following difficulties: 1. The content of ash, metal impurities and free carbon powder in coal tar is high. If the whole fraction or heavy fraction of coal tar is directly hydrogenated by trickle bed process, it is easy to cause catalyst bed The layer pressure drop increases; two, the heat release during the coal tar h...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G67/00
Inventor 李华李庆华佘喜春朱方明刘呈立曾志煜
Owner HUNAN CHANGLING PETROCHEM SCI & TECH DEV CO LTD