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Fluidized bed reactor and application thereof, and method for adsorbing and desulfurizing hydrocarbon oil

A fluidized bed reactor, adsorption desulfurization technology, applied in chemical instruments and methods, processing hydrocarbon oil, refining hydrocarbon oil, etc., can solve the problems of rapid rise in pressure drop of metal filters, broken catalyst, large amount of fine powder, etc. , to achieve the effect of prolonging the operation period of the device, delaying the clogging time and high separation efficiency

Active Publication Date: 2018-10-02
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0009] Cyclone separator is a kind of solid powder commonly used to separate dust-containing gas and reduce the concentration of solid powder in dust-containing gas. However, compared with other solid catalysts, the mechanical strength of the catalyst for adsorption desulfurization is slightly lower. If In the adsorption desulfurization reactor, a conventional cyclone separator is used to pre-separate the dilute-phase suspended dust-containing gas in the desulfurization adsorption reactor. Due to the high flow rate of the gas flow in the cyclone separator, when separating oil gas and catalyst particles, particles and Strong collisions between particles and between particles and the wall of the cyclone separator can easily cause catalyst breakage
On the contrary, a large number of catalysts are broken, resulting in more fine powder in the fluidized bed reactor and faster catalyst consumption; the load on the metal filter is greater, which is more likely to cause a rapid increase in the pressure drop of the metal filter

Method used

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  • Fluidized bed reactor and application thereof, and method for adsorbing and desulfurizing hydrocarbon oil
  • Fluidized bed reactor and application thereof, and method for adsorbing and desulfurizing hydrocarbon oil
  • Fluidized bed reactor and application thereof, and method for adsorbing and desulfurizing hydrocarbon oil

Examples

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Embodiment 1

[0069] use Figure 4 The shown adsorption desulfurization reaction device performs adsorption desulfurization reaction on sulfur-containing hydrocarbon raw materials. In the fluidized bed reactor, the diameter of the upper fine powder filtering space III is 200mm, and the diameter of the dense phase bed layer I of the reactor is 160mm. The height of the space is 5000mm, and the apex angle of the three-layer cone in the reactor is 86.3°; a particle sorter is set in the fluidized bed reactor, the main body height of the particle sorter is 150mm, and 3 air inlets, The diameter of the outer layer guide body 2 of the particle pre-separator is 78 mm, the cylinder height is 94 mm, the cone height is 152 mm, the diameter d3 of the outer layer guide body feeding pipe 13 = 32 mm, and the diameter d2 of the inner fine powder collection cone feeding pipe 9 =32mm, its end is apart from the height 110mm of outer layer diversion body 2 top plates, the diameter d1=16mm of secondary layer dive...

Embodiment 2

[0076] Adsorption desulfurization reaction is carried out in the same method as in Example 1. The apex angle of the triple cone, the distance between the cones, and the diameter of the discharge material 13 are all the same. The difference is that four air inlets are used, and the inlet area is A1 =0.000968m 2 , the inner layer fine powder collection cone feeding pipe 9 is d1=14mm, the inner diameter of the opening 8 at the bottom of the secondary diversion cone is d2=30mm, and the distance h=100mm from its end to the top plate of the outer layer diversion body 2, the outer layer diversion body enters The tuyere area is 0.00055m 2 ; The average gas velocity of the reactor barrel section is 0.34m / s, and the linear velocity at the air inlet of the particle pre-separator is 7.07m / s, and the average linear velocity at the annular mouth at the bottom of the secondary diversion cone is 12.4m / s s.

[0077] During the reaction, the composition of the obtained oil and gas product, th...

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Abstract

The invention relates to a fluidized bed reactor and an application thereof, and a method for adsorbing and desulfurizing hydrocarbon oil, the fluidized bed reactor comprises a lower dense phase bed layer and an upper sparse phase bed layer, wherein the sparse phase bed layer is internally provided with a particle pre-separator and an inner layer fine powder collecting cone (5) ; the particle pre-separator consists of an outer layer flow deflector (2) and a secondary layer diversion cone (4), wherein the outer layer flow deflector (2) is composed of a top plate, a straight cylinder section, acone section and an outer layer flow deflector feeding pipe (13), an air inlet (3) is arranged on the side surface of the straight cylinder section, the conical skirt edge of the secondary layer diversion cone is seamlessly connected with the reactor cylinder body, and the bottom opening of the conical skirt edge is in the outer layer flow deflector; the top of the inner layer fine powder collecting cone (5) is connected with the reaction cylinder body through a rib plate; the bottom openings of the outer layer flow deflector feeding pipe (13) and the inner layer fine powder collecting cone feeding pipe (9) are in the dense phase bed layer. In the application process of the fluidized bed reactor, the abrasion in the separation process of the particles can be reduced, and the operation period of the device is prolonged.

Description

technical field [0001] The invention relates to a fluidized bed reactor and its application, more specifically, to a fluidized bed reactor for pre-sorting catalyst particles and its application. Background technique [0002] Fuel oil always contains some organic sulfur. These organic sulfurs release SO when burned x , the most important of which is sulfur dioxide. 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. Countries and regions such as Europe and the United States first proposed the "sulfur-free gasoline" standard with a gasoline sulfur content of ≯10μg / g, and my country is also fully implementing the National IV and V gasoline standards recently. [0003] At present, there are mainly two methods for deep desulfurization of oil products: hydrorefining and adsor...

Claims

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Application Information

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IPC IPC(8): B01J8/24C10G25/09
CPCB01J8/0055B01J8/007B01J8/24C10G25/09C10G2300/202
Inventor 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