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Adsorption desulfurization reaction device and adsorption desulfurization method

A technology of adsorption desulfurization and reaction device, which is applied in the petroleum industry, refining hydrocarbon oil, etc., can solve the problems of catalyst crushing, coarse and fine particle entrainment, catalyst consumption, etc., and achieve low probability of secondary crushing, stable long-term operation, and stable desulfurization effect of effect

Active Publication Date: 2014-05-14
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the metal filter has a small pore size and is mainly used to recover fine powder, while solid particles larger than 2 μm in the catalyst tend to remain in the reaction system, resulting in a large number of small catalyst fine particles that cannot be removed from the reactor in time. Desulfurization effect of the device
Moreover, with the accumulation of catalyst fine particles in the reaction system, the solid phase density of the catalyst bed is greatly reduced, which breaks the pressure balance in the reaction system, resulting in insufficient catalyst flow driving force, which cannot make the catalyst flow into the reaction receiver normally. , causing the catalyst to flow poorly and affecting the normal operation of the device
[0010] Compared with other solid catalysts, the mechanical strength of the catalyst for adsorption desulfurization is slightly lower. If a conventional cyclone separator is installed in the adsorption desulfurization reactor to separate the catalyst, due to the high flow rate of the gas flow in the cyclone separator, it is difficult to separate oil and gas. When contacting catalyst particles, the strong collision between particles and between particles and the wall of the cyclone separator can easily cause the catalyst to break
Moreover, the cyclone separator is a highly turbulent centrifugal force field, and the turbulence intensity of the large and small particles is different, which leads to serious entrainment of coarse and fine particles during the separation process, and the boundary definition of particle separation is limited, so it is impossible to separate the catalyst in the fluidized bed reactor into fine particles. The fine powder is effectively sorted out, and a large amount of catalyst is broken, resulting in more fine powder in the fluidized bed reactor and faster catalyst consumption

Method used

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  • Adsorption desulfurization reaction device and adsorption desulfurization method

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Embodiment 1

[0091] In this embodiment, four guiding air inlets (such as figure 2 As shown, the guide air inlet is set along the circumference of the straight cylinder area, and each guide air inlet has the same cross-sectional area perpendicular to the airflow direction), and three guides are arranged tangentially on the air outlet pipe of the airflow particle separator air outlet (such as figure 2 As shown, the guide air outlet is set along the circumference of the air outlet pipe, and the area of ​​each guide air outlet perpendicular to the air flow direction section is the same); the difference between the area of ​​the horizontal section of the straight barrel area and the area of ​​the horizontal section of the air outlet pipe for A 0 , the total area of ​​the cross-section perpendicular to the air flow directed to the air inlet is A 1 , the total area of ​​the cross-section perpendicular to the air flow directed to the air outlet is A 2 , A 1 / A 0 0.4:1, A 2 / A 0 is 0.2:1; ...

Embodiment 2

[0106] Adopt the method identical with embodiment 1 to carry out adsorption desulfurization, difference is, A 1 / A 0 0.24:1, A 2 / A 0 is 0.15:1, the linear velocity of the oil mixture at the guide air inlet of the airflow particle separator is 2.5m / s, and the linear velocity at the guide air outlet of the airflow particle separator is 4m / s.

[0107] Continuously for 500 hours. During the reaction, the composition of the obtained oil and gas product and the average particle size of the catalyst in the catalyst fine powder storage tank and the catalyst dense bed in the fluidized bed reactor were monitored, and the results are listed in Table 4. After reacting for 500 hours, the content of the catalyst with a particle size of less than 30 μm in the catalyst in the dense-phase bed in the fluidized bed reactor was 9.5% by weight. A total of 14.2kg of catalyst was loaded in the fluidized bed reactor before the reaction started, and 1.34kg of catalyst was added to the fluidized b...

Embodiment 3

[0123] Adopt the method identical with embodiment 1 to carry out adsorption desulfurization, difference is:

[0124] There are 6 guiding air inlets (such as figure 2 As shown, the guide air inlet is arranged along the circumference of the straight cylinder area, and each guide air inlet has the same cross-sectional area perpendicular to the air flow direction), and 6 guide guides are arranged tangentially on the air outlet pipe of the airflow particle separator air outlet (such as figure 2 As shown, the guide air outlet is set along the circumference of the air outlet pipe, and the area of ​​each guide air outlet perpendicular to the air flow direction section is the same); the difference between the area of ​​the horizontal section of the straight barrel area and the area of ​​the horizontal section of the air outlet pipe for A 0 , the total area of ​​the cross-section perpendicular to the air flow directed to the air inlet is A 1 , the total area of ​​the cross-section ...

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Abstract

The invention discloses an adsorption desulfurization reaction device, a fluidized bed reactor of the adsorption desulfurization reaction device is provided with a pneumatic particle sorting device which comprises a sorting device main body, a discharge port, a wind outlet pipe and a guide wind inlet; the interior space of the sorting device main body comprises, from top to bottom, a straight cylinder area and a pyramidal area, the discharge port is located at the bottom of the pyramidal area, the guide wind inlet is arranged, along the tangent direction of the straight cylinder area, on the upper part of the straight cylinder area, the wind outlet pipe is inserted into the sorting device main body in a sealing manner, and extends to the lower part of the straight cylinder area, the bottom end port of the wind outlet pipe is sealed, and a guide wind outlet is arranged, along the tangential direction, on the lower part of the wind outlet pipe. The invention also discloses an adsorption desulfurization method performed in the adsorption desulfurization reaction device. According to the adsorption desulfurization method, catalyst fine powder produced in an adsorption desulfurization process can be timely transferred out of the fluidized bed reactor; and in the separation and sorting process, the secondary damage rate of catalyst particles is low, so that the adsorption desulfurization method can obtain good and stable desulfurization effects.

Description

technical field [0001] The present invention relates to an adsorption desulfurization reaction device, and also relates to an adsorption desulfurization method using the above adsorption desulfurization reaction device. Background technique [0002] Petroleum hydrocarbons such as gasoline and diesel always contain some organic sulfur. These organic sulfurs release SO when burned x , the most important of which is sulfur dioxide (SO 2 ). Sulfur dioxide is the main pollution source of the atmospheric environment and the direct cause of acid rain. In order to control air pollution, countries successively put forward stricter restrictions on the sulfur content in gasoline through legislation. Europe, the United States and other countries and regions have proposed the "sulfur-free gasoline" standard with gasoline sulfur content ≯10μg / g. [0003] At present, there are mainly two methods for deep desulfurization of oil products: hydrorefining and adsorption desulfurization. Ho...

Claims

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Application Information

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IPC IPC(8): C10G25/00C10G25/12
Inventor 龙军田志鸿侯栓弟武雪峰张久顺毛安国张哲民朱丙田
Owner CHINA PETROLEUM & CHEM CORP
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