Hydrocracking method for processing low-sulfur raw material

A technology for hydrocracking and raw materials, applied in hydrotreating process, petroleum industry, processing of hydrocarbon oil, etc., can solve the problems of gas blockage of raw oil pump, difficulty in long-term operation, consumption of vulcanizing agent, etc., so as to improve product quality and save equipment. The effect of low investment and operating costs

Active Publication Date: 2014-05-21
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although this method can ensure the activity of the catalyst, it will increase material consumption, human consumption, energy consumption, etc.
[0005] CN99112819.2 introduces a method for supplementing sulfur in a paraffin hydrorefining method. Although the hydrogenation activity of the sulfurized hydrogenation catalyst can be restored without stopping the device, a certain amount of sulfurizing agent is required to be consumed additionally.
[0006] CN93121026.7 introduces a sulfur replenishing method. Although the hydrocarbon oil sulfur replenishing method can ensure catalyst activity, it needs to consume a certain amount of hydrocarbon oil. Although the gas sulfur replenishing method does not need to consume hydrocarbon oil, it requires additional The system injects hydrogen sulfide into the reaction part, which consumes a lot of energy, and at the same time, it is easy to cause air resistance in the raw material oil pump, making it difficult to operate for a long time

Method used

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  • Hydrocracking method for processing low-sulfur raw material
  • Hydrocracking method for processing low-sulfur raw material

Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach

[0024] Such as figure 1 Shown, a kind of implementation mode of combined hydrogenation process flow of the present invention is as follows:

[0025] The high-sulfur raw material 1 is mixed with hydrogen gas 30 and then enters the hydrotreating unit 2, the reaction effluent 3 enters the hot high-pressure separator 4, the liquid 6 obtained by the hot high-resolution is sent to the fractionation tower, the obtained gas 7 is injected into the washing water 8, and is cooled by high-pressure air After the reactor 9, it enters the cold high-pressure separator 10, and the waste liquid 11 containing sulfide amine and hydrosulfide amine is separated, and the hydrogen-rich gas 12 enters the circulating hydrogen desulfurization tower 13 and contacts with the lean amine liquid 15, and the obtained rich amine liquid 14 is discharged for desulfurization The tower enters the regeneration system, and at the same time obtains hydrogen-rich gas 16 with a certain concentration of hydrogen sulfide...

Embodiment 1

[0030] use figure 1 In the process flow shown, the hydrotreating unit for processing high-sulfur raw material 2 and the circulating hydrogen path of hydrocracking unit for processing low-sulfur raw material 1 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 the hydrogenation process are shown in Table 3, and the concentration of hydrogen sulfide in circulating hydrogen, DMDS consumption, injection cycle of lean amine solution and unit operation cycle are shown in Table 4.

[0032] Table 1 Main physicochemical properties of the catalyst

[0033] project

FF-36

FC-14

FF-14

Appearance shape

Clover Strips

Cylindrical bar

Clover Strips

Particle diameter, mm

1.1~1.3

1.5~1.7

1.1~...

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Abstract

The invention discloses a hydrocracking method for processing a low-sulfur raw material. The method comprises the steps of: hydroprocessing a high-sulfur raw material, and performing gas-liquid separation on a reaction effluent to obtain sulfur-containing hydrogen-enriched gas; hydrocracking low-sulfur raw oil, and performing gas-liquid separation on a reaction effluent to obtain a low-sulfur hydrogen-enriched gas; and mixing the sulfur-containing hydrogen-enriched gas and the low-sulfur hydrogen-enriched gas, selectively performing hydrogen sulfide removal treatment on the gas mixture, and circulating the treated gas mixture to a reactor inlet. According to the invention, two paths of hydrogen-enriched gas of the hydroprocessing process and the hydrocracking process are effectively combined, and the sulfur-containing hydrogen-enriched gas subjected to hydroprocessing is fully utilized to replenish sulfur for a low-sulfur raw material hydrocracking device, so that the problem of sulfur loss of the catalyst during long-term operation of the low-sulfur hydrocracking device is effectively solved. The hydrocracking method disclosed by the invention has the advantages of simplified process flow, low operation cost, low total investment and the like.

Description

technical field [0001] The invention relates to a combined hydrogenation process, mainly referring to the combination of a hydrogenation treatment unit and a hydrocracking unit, especially a hydrocracking unit used for processing low-sulfur raw materials. Background technique [0002] Hydrocracking is a catalytic conversion process in which heavy distillate oil undergoes hydrogenation, desulfurization, denitrogenation, rearrangement of molecular skeleton structure and cracking in the presence of high temperature and high pressure hydrogen and catalyst. It has many advantages such as strong raw material adaptability, flexible product scheme, high yield of liquid products, and good product quality. It has been favored by oil refining companies all over the world for many years. As one of the main processes for deep processing of heavy oil, hydrocracking can not only directly produce clean motor fuels such as gasoline, coal, and diesel, but also light and heavy naphtha and hydr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G65/14
Inventor 王仲义太史剑瑶刘继华石友良刘涛黄新露孙士可
Owner CHINA PETROLEUM & CHEM CORP
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