Concave flow distribution plate and reactor with same

An air distribution plate and air distribution technology, which is applied in chemical instruments and methods, chemical/physical processes, etc., can solve the imbalance of circumferential flow and axial flow, cannot form a three-dimensional bed as a whole, and the force of a circular plate is stronger than that of a shell. Body difference and other problems, to achieve the effect of no dead zone, safe and scientific space layout, and safe protection of the shell wall

Active Publication Date: 2016-10-26
THE CHALLENGE PETROCHEM MACHINERY CORP
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The distribution plate is a circular plate-shaped structure, and there are two main problems: one is that the production capacity is limited, and two kinds of through holes need to be designed on the same plate. The granular products on the top flow down smoothly through the through hole. With the increase of production capacity, the two channels of ascending and descending will be randomly blocked; second, the side of the circular plate bears less force than the shell and is easy to deform. The structure and airflow deviated from the original design
[0009] One is the three-dimensional non-equilibrium of the process gas fluidized bed. The process gas forms a spirally rising air flow in the funnel of the distribution plate. The energy loss of the swirling flow in the upward movement causes the circumferential flow state and the axial flow state to be unbalanced, so that from The material from top to bottom gradually generates particles during the reaction, and the coarse particles flow to the surrounding shell wall under the centrifugal action of the swirling flow, which easily causes the radial flow state to be unbalanced
Second, it is difficult to control the airflow pressure at the opening of the distribution plate. This is because the funnel-shaped inverted conical structure makes the space under the distribution plate gradually expand during the rising process, and the process gas under the distribution plate is rising. In the process, the total amount of process gas under the distribution plate is gradually reduced because part of it flows

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  • Concave flow distribution plate and reactor with same
  • Concave flow distribution plate and reactor with same
  • Concave flow distribution plate and reactor with same

Examples

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Example Embodiment

[0038] Example 1

[0039] One of the specific embodiments of a concave air distribution plate of the present application, refer to figure 1 with figure 2 As shown, it is formed by an improvement of a flat air distribution plate. The innovation of the present application is that the concave air distribution plate 10 includes a concave structure recessed downward along the central axis of the concave air distribution plate 10 11, and a bending structure 12 formed by bending the circumferential side of the concave air distribution plate 10 downward.

[0040] Specifically, the concave structure 11 is an inverted cone structure. The concave air distribution plate 10 is composed of a concave structure in the middle and a bent structure 12 on the peripheral side to form an M-shaped air distribution plate. Research shows that the M-shaped structure has radial elasticity and can adapt to the deformation of the reactor. Displacement without being twisted and deformed, so its periphery can ...

Example Embodiment

[0050] Example 2

[0051] The second embodiment of a concave air distribution plate of the present application. The main technical solution of this embodiment is the same as that of Embodiment 1. For the features not explained in this embodiment, the explanation in Embodiment 1 is adopted. Do not repeat it. reference image 3 As shown, the difference between this embodiment and Embodiment 1 is that the concave structure 11 is a spherical structure 16. The process gas can be evenly distributed in the reactor to flow upwards, and at the same time, the generated material particles can be collected and discharged from the bottom through the concave air distribution plate. It can also resist the vibration fatigue caused by the large flow rate and the fast gas flow rate. An anti-deposition distribution plate that meets pressure drop stability and good fluidization quality.

Example Embodiment

[0052] Example 3

[0053] The third specific implementation manner of a concave airflow distribution plate of the present application. The main technical solution of this embodiment is the same as that of Embodiment 1. For the features not explained in this embodiment, the explanation in Embodiment 1 is adopted. Do not repeat it. reference Figure 4 As shown, the difference between this embodiment and Embodiment 1 is that the concave structure 11 is a concave structure 17 composed of symmetrically arranged inner convex hyperboloids. The process gas can be evenly distributed in the reactor to flow upwards, and at the same time, the generated material particles can be collected and discharged from the bottom through the concave air distribution plate. It can also resist the vibration fatigue caused by the large flow rate and the fast gas flow rate. An anti-deposition distribution plate that meets pressure drop stability and good fluidization quality.

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Abstract

The application relates to a concave flow distribution plate and a reactor with the same. The concave flow distribution plate is formed by modifying a flat flow distribution plate and comprises a concave structure that is concave down along its axis and a bent structure bent down from the periphery of the concave flow distribution plate; the concave structure is conical structure, spherical structure or composed of symmetrical concave double-curved surface; the flow distribution plate helps process gas from the bottom of the reactor to flow out of flow holes so that material from the upper portion of the reactor and process gas rising from below can be balanced and fully contacted, thus keeping a relative pressure, the distribution plate has flow balancing performance, particulate mobility and internal structure fatigue resistance and is simple in combination structure and convenient to mount and maintain, a support of the distribution plate is more reasonably stressed, high stability is provided, spatial layout is safer and more scientific, the reactor is better in operation flexibility, reaction heat can be removed more flexibility, safety of a shell wall is protected, and the service life of the reactor is prolonged.

Description

technical field [0001] This application relates to the technical field of various large-scale high-grade reactors used in petroleum refining and chemical industry, coal chemical industry, chemical fertilizer industry and other various chemical equipment, such as fluidized bed gas phase reactor, hydrogenation through catalyst reaction A reactor or a desulfurization reactor, etc., especially relates to a concave air flow distribution plate and a reactor thereof. Background technique [0002] A chemical reactor, including a cylinder, a head arranged at both ends of the cylinder, a material inlet and outlet arranged on the head, an airflow distribution plate inside the cylinder and an inner support structure for supporting the airflow distribution plate, or a cylinder The supporting structure of the catalyst in the body also includes a surfacing corrosion-resistant lining on the inner surface of the pressure vessel. [0003] In recent years, with the development of petrochemica...

Claims

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Application Information

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IPC IPC(8): B01J8/18
CPCB01J8/1827B01J8/1872B01J2208/00938
Inventor 陈孙艺卢学培张骞
Owner THE CHALLENGE PETROCHEM MACHINERY CORP
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