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
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
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...
PUM
| Property | Measurement | Unit |
|---|---|---|
| Diameter | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 


