Gasoline fraction desulfurization method, method for producing low-sulfur gasoline and reaction system

A gasoline fraction and reaction system technology, which is applied in the petroleum industry, hydrocarbon oil treatment, hydrotreating process, etc., can solve the problems of small adjustable range of reaction conditions and reduced operation flexibility of the device, so as to save equipment investment and save energy. Energy consumption and equipment investment, the effect of suppressing the generation of regenerated mercaptan

Active Publication Date: 2021-04-16
CHINA PETROLEUM & CHEM CORP +1
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Problems solved by technology

However, this method also has disadvantages. Firstly, the product after primary hydrodesulfurization still needs to be separated from gas and liquid through a high-pressure separation tank, and the obtained liquid phase enters the stripping tower again, and there is still energy consumption caused by material phase change and temperature rise and fall; secondly ...

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  • Gasoline fraction desulfurization method, method for producing low-sulfur gasoline and reaction system

Examples

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Embodiment 1

[0075] Embodiment 1 adopts the accessory provided by the present invention figure 1 In the flow chart of the method for producing low-sulfur gasoline shown, the raw materials used are the same as those of the comparative example, and the primary desulfurization reaction conditions of the first reactor and the catalyst used are the same as those of the comparative example 1. The reaction product of the first reactor is heated to 180°C and then enters the stripping tower. The operating pressure of the stripping tower is 1.6MPa, the temperature at the top of the tower is 40°C, and the temperature at the bottom of the tower is 180°C. 8 pieces. The second reactor is a heat exchange reactor with a shell and tube structure. The second hydrodesulfurization catalyst is filled in the tube side of the reactor. The preparation method of the second hydrodesulfurization catalyst refers to the published patent CN104437518A. Into medium pressure steam heating. The operating conditions of th...

Embodiment 2

[0077] Embodiment 2 adopts the method for producing low-sulfur gasoline according to the present invention, the raw materials used are the same as those of the comparative example, the cutting temperature of the whole distillate gasoline is 70° C., and the steps and conditions of the alkali washing desulfurization of the cut light gasoline fraction are the same as those of the comparative example 1. Gasoline fraction and hydrogen by volume ratio 400Nm 3 / m 3 After mixing, it is heated to 280°C by a heat exchanger and a heating furnace and enters the first reactor. The operating conditions are: reaction pressure 1.8MPa, and the volumetric space velocity of the feed liquid is 6h -1 . The reaction product of the first reactor is heated to 180°C and then enters the stripping tower. The operating pressure of the stripping tower is 1.6MPa, the temperature at the top of the tower is 40°C, and the temperature at the bottom of the tower is 185°C. 8 pieces. The secondary desulfurizat...

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Abstract

The invention relates to a gasoline fraction desulfurization method, a method for producing low-sulfur gasoline and a reaction system. According to the method, a gasoline fraction enters a first reactor, and contacts a first hydrodesulfurization catalyst in the presence of hydrogen to carry out a first hydrodesulfurization reaction; a product obtained after the reaction enters a steam stripping tower, hydrogen-rich gas containing hydrogen sulfide and an intermediate gasoline fraction are obtained at the top of the steam stripping tower, a descending tower bottom material enters a second reactor and contacts a second desulfurization catalyst to be subjected to a secondary desulfurization reaction, a reaction product returns to the bottom of the steam stripping tower, a liquid phase in the reaction product is extracted to serve as a desulfurized heavy gasoline fraction, and a vapor phase returns to the steam stripping section of the steam stripping tower; and the second reactor is a heat exchange type reactor, and an external heat source flows through a coil pipe or a tube nest in the heat exchange type reactor to heat reaction materials. The gasoline fraction desulfurization method provided by the invention can reduce energy consumption, and is small in octane number loss and high in desulfurization depth.

Description

technical field [0001] The invention relates to a method and a reaction system for desulfurizing hydrocarbon oil, more specifically, to a method and a reaction system for removing sulfur compounds in gasoline fractions. Background technique [0002] As people pay more and more attention to the harmful substances emitted by automobile exhaust, countries all over the world have put forward strict requirements on the quality of automobile fuel. my country's National V Motor Gasoline Standard, which has been implemented in January 2017, and the National VI Motor Gasoline Standard scheduled to be implemented in January 2019 both require that the sulfur content be less than 10 μg / g. In order to meet the new standards, domestic refineries are faced with the task of transforming and upgrading the clean gasoline production process. my country's motor gasoline is mainly composed of catalytic cracking gasoline, accounting for about 80% of finished gasoline. However, its sulfur conten...

Claims

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Application Information

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IPC IPC(8): C10G67/02C10G67/00
Inventor 黄涛庞博袁清刘锋毛俊义李明丰王雷
Owner CHINA PETROLEUM & CHEM CORP
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