Integrated hydroprocessing method

A technology for hydrotreating and treating zone, applied in hydrotreating process, treating hydrocarbon oil, petroleum industry, etc., can solve the problems of complicated operation, low total income, high energy consumption and material consumption, etc., to simplify the process flow, reduce The effect of low total consumption and operating costs

Active Publication Date: 2014-07-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] At present, due to the need to process high-sulfur raw materials, the catalytic hydrogenation units of most oil refineries will add a circulating hydrogen desulfurization tower to their high-pressure gas lines. The operation of this tower can effectively control the hydrogen sulfide concentration in the circulating hydrogen and improve the efficiency of the reaction system. Hydrogen partial pressure, thereby reducing the steam energy consumption of the circulating hydrogen compressor and reducing the corrosion of the compressor and other equipment caused by the circulating hydrogen, but it will increase the primary investment of the device, and will continue to consume lean amine liquid during the operation of the device, although There is a solvent regeneration system, but the energy consumption and material consumption are still relatively large, which will inevitably lead to a decrease in total revenue
CN1962829A introduces the production method of clean oil, but the operation is relatively complicated; CN101455933A and CN101434381A introduce the tower top purification device and purification method of the circulating hydrogen desulfurization tower, but they all belong to follow-up work, and the investment is relatively large, and they cannot solve the problem of circulating hydrogen at present. Consumption of lean amine solution and large energy consumption in the desulfurization tower

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] use figure 1 In the process flow shown, the circulating hydrogen paths of hydrotreating units A and B are organically combined. The properties of the catalysts used in the examples are listed in Table 1. The catalyst is a commercial catalyst developed and produced by Fushun Petrochemical Research Institute.

[0031] The properties of raw oil are shown in Table 2, the operating conditions of hydrotreating are shown in Table 3, and the gas composition and the replenishment period of lean amine solution after mixing high-fraction gas with water are shown in Table 3.

[0032] Table 1 Main physicochemical properties of the catalyst

[0033] catalyst

FF-14

FF-46

Physical properties:

Pore ​​volume, mL / g

0.341

>0.33

Specific surface, m 2 / g

167

>160

Packing density, g / cm 3

0.955

~0.90

Compressive strength, KN / grain

15.9

≥150

Chemical composition, wt%:

...

Embodiment approach

[0040] Such as figure 2 As shown, another embodiment of the combined hydroprocessing method of the present invention is as follows:

[0041] The high-sulfur diesel raw material 1 is mixed with hydrogen 25 and enters the hydrotreating unit 27, and the reaction effluent 3 enters the thermal high-pressure separator 4 (referred to as thermal high-resolution), and the liquid 6 obtained by the thermal high-resolution is sent to the fractionation tower; the high-nitrogen raw material 7 is mixed with After the hydrogen gas 25 is mixed, it enters the hydrocracking unit 28, and the obtained reaction effluent 9 enters the heat fraction 10 for separation, and the obtained liquid 12 goes to the fractionation tower; the gas 5 obtained from the heat fraction 4 is mixed with the gas 11 obtained from the heat fraction 10 Afterwards, gas 13 is formed, and the gas 13 is injected into the washing water 14. After passing through the high-pressure air cooler 15, it enters the cold high-pressure se...

Embodiment 2

[0046] use figure 2 In the process flow shown, the circulating hydrogen paths of the hydrorefining unit A and the hydrocracking unit B are organically combined. The properties of the catalysts used in the examples are listed in Table 5. The catalyst is a commercial catalyst developed and produced by Fushun Petrochemical Research Institute.

[0047] The properties of raw oil are shown in Table 6, the operating conditions of hydrotreating are shown in Table 7, and the gas composition after mixing high-fraction gas and washing with water and the replenishment cycle of lean amine solution are shown in Table 8.

[0048] Table 5 Main Physicochemical Properties of Catalysts

[0049] project

FF-36

FC-14

Appearance shape

Clover Strips

Cylindrical bar

Particle diameter, mm

1.1~1.3

1.5~1.7

Strip length, mm

3~8

3~8

Crushing strength, N / cm

≥180

>185

Chemical composition, m%:

M...

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Abstract

The invention discloses an integrated hydroprocessing method. The method includes the following steps: under hydroprocessing conditions, high-sulfur raw oil and hydrogen are mixed and then pass through a hydroprocessing catalyst bed, high-nitrogen raw oil and hydrogen are mixed and then pass through a hydroprocessing catalyst bed, reaction effluents respectively enter hot high-pressure separators and are separated, two routes of produced gas are mixed and injected into washing water and then enter a cold high-pressure separator via a high-pressure air cooler, and the produced hydrogen-rich gas is recycled after passing through a circulating hydrogen desulfurization tower. The integrated hydroprocessing method organically combines hydroprocessing processes for processing different natures of materials, consequently, on the basis of the normal processing of different natures of poor-quality materials, the respective characteristics of the materials can be sufficiently utilized, and thereby an ideal comprehensive processing effect can be achieved. The method integrates two gas routes together, and has the advantages of little equipment investment, lower operation cost, simplified process flow and the like.

Description

technical field [0001] The invention relates to a combined hydrogenation method, mainly referring to the combination of hot and high-separation gas paths, which is suitable for various catalytic hydrogenation methods for separately processing high-nitrogen raw materials and high-sulfur raw materials. Background technique [0002] Catalytic hydrogenation is of great significance for improving the processing depth of crude oil, rationally utilizing petroleum resources, improving product quality, increasing light oil yield and reducing air pollution. Especially as crude oil becomes heavier and worse, there is an increasing demand for middle distillates, and catalytic hydrogenation has become an important process in petroleum processing. In addition, due to the increase of sour crude oil, catalytic hydrogenation is more important. Catalytic hydrogenation is a general term for catalytic processing of petroleum fractions in the presence of hydrogen. Currently, there are two main...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G65/14
Inventor 王仲义太史剑瑶刘涛刘继华黄新露孙士可桂兴华
Owner CHINA PETROLEUM & CHEM CORP
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