Novel reactor capable of realizing efficient distribution of fed materials

Abstract

The utility model provides a novel reactor capable of realizing efficient distribution of fed materials. The novel reactor comprises a vertical distributor (2) and an annular distributor (3) which are arranged in a reactor (1), wherein the annular distributor (3) is arranged on the central axis in the reactor (1), and a second gas outlet (31) which is vertically and upwards formed is formed in the annular distributor (3); the vertical distributor (2) is arranged between the annular distributor (3) and the inner side wall of the reactor (1), and a first gas outlet (21) which is horizontally formed is formed in the vertical distributor (2).

Description

Technical Field

[0001] This utility model relates to a reactor, and more particularly to a novel reactor that can achieve efficient feed distribution. Background Technology

[0002] This section provides only background information relevant to this disclosure and is not necessarily prior art.

[0003] In chemical production, gas-liquid reaction is a common process. Most gas-liquid reactions are carried out in batch reactors, accompanied by stirring and jacketing to ensure sufficient reaction and meet heating or cooling requirements. However, some special reactions require specific reaction pressures, and stirring can reduce the reactor's sealing performance. Furthermore, stirring increases energy consumption.

[0004] In existing technologies, the use of ordinary ring distributors results in insufficient stirring, leading to incomplete reaction and reduced reaction efficiency.

[0005] It should be noted that the information disclosed in the background section above is only used to enhance the understanding of the background of this disclosure, and therefore may include information that does not constitute prior art known to those skilled in the art. Utility Model Content

[0006] Purpose of the invention: The technical problem to be solved by this invention is to provide a novel reactor that can achieve efficient feed distribution, addressing the shortcomings of existing technologies.

[0007] To address the aforementioned technical problems, this utility model discloses a novel reactor capable of achieving efficient feed distribution, comprising:

[0008] Vertical and annular distributors are installed in the reactor; among them,

[0009] The annular distributor is located on the central axis inside the reactor, and the annular distributor is provided with a second air outlet that is opened vertically upward.

[0010] The vertical distributor is disposed between the annular distributor and the inner wall of the reactor, and the vertical distributor is provided with a first horizontally opened air outlet.

[0011] Furthermore, the number of vertical distributors is one or more. When the number of vertical distributors is two or more, the vertical distributors are evenly distributed around the annular distributor.

[0012] Furthermore, the vertical distributor includes:

[0013] A first air inlet connection flange is provided below the bottom of the reactor, and a first bolt hole is provided on the first air inlet connection flange for installation and connection with an external air supply device.

[0014] A vertical main pipe is fixed above the first air inlet connection flange. The vertical main pipe has a hollow cylindrical structure. The bottom of the vertical main pipe is open and fixedly connected to the top of the first air inlet connection flange. The upper part of the vertical main pipe runs vertically through the inside of the reactor, and the top of the vertical main pipe is closed. The vertical main pipe is located inside the reactor and has a first air outlet.

[0015] Furthermore, the first air outlet is opened outward along the tangential direction of the outer wall of the vertical main pipe.

[0016] Furthermore, the first air outlet has multiple openings, among which the first air outlets on the same horizontal plane are in a single layer.

[0017] Furthermore, the first air outlet is configured with multiple layers.

[0018] Furthermore, the ring distributor includes:

[0019] A main air inlet pipe extends horizontally out of the outer wall of the reactor, with one end of the main air inlet pipe located inside the reactor and connected to the bottom end of a vertically installed vertical connecting pipe;

[0020] A distribution ring is horizontally arranged on the outside of the vertical connecting pipe, and the distribution ring is connected to the vertical connecting pipe through a horizontally arranged horizontal connecting pipe; the second air outlet is opened on the distribution ring, and the opening direction is vertically upward.

[0021] Furthermore, the horizontal connecting pipes are configured in multiple layers, evenly distributed between the vertical connecting pipes and the distribution ring; the distribution ring is configured in multiple layers.

[0022] Furthermore, the main air inlet pipe is located at one end outside the reactor and is fixedly provided with a second air inlet connection flange. The second air inlet connection flange is provided with a second bolt hole for installation and connection with an external air supply device.

[0023] Furthermore, the first air outlet is square; the second air outlet is circular.

[0024] Beneficial effects:

[0025] 1. The vertical distributor proposed in this utility model is equipped with a square air outlet with a large area, which forms a tangential force and can drive the liquid phase to rotate, thereby achieving the purpose of thorough stirring.

[0026] 2. The annular distributor proposed in this utility model has a circular air outlet at the top. Under the action of gas phase pressure, it forms an upward force, which drives the liquid to move upward and increases the thoroughness of stirring.

[0027] 3. The combined action of the annular distributor and the vertical distributor proposed in this utility model has both a horizontal annular force to drive the liquid phase to rotate and stir, and a vertical upward force to achieve the effect of stirring from top to bottom, so that the gas and liquid are mixed more fully and evenly.

[0028] 4. The reactor proposed in this utility model eliminates the stirring device, saving power consumption, while reducing sealing leakage points and improving sealing performance. Attached Figure Description

[0029] The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments, and the advantages of the present invention in the above and / or other aspects will become clearer.

[0030] Figure 1 This is a schematic diagram of the overall structure of this utility model.

[0031] Figure 2 This is a top view of the present invention.

[0032] Figure 3 This is a side view of a vertical distributor.

[0033] Figure 4 This is a top view of the vertical distributor.

[0034] Figure 5 This is a schematic diagram of a ring distributor.

[0035] Figure 6 This is a side view of the ring distributor.

[0036] Figure 7 This is a schematic diagram of the air outlet distribution of the annular distributor.

[0037] In the diagram, 1 is the reactor, 2 is the vertical distributor, and 3 is the annular distributor; 21 is the first air outlet, 22 is the first air inlet connection flange, 23 is the first bolt hole, and 24 is the vertical main pipe; 31 is the second air outlet, 32 is the second air inlet connection flange, 33 is the second bolt hole, 34 is the distribution ring, 35 is the main air inlet pipe, 36 is the vertical connecting pipe, and 37 is the horizontal connecting pipe. Detailed Implementation

[0038] This invention addresses the shortcomings of insufficient stirring and uneven reaction by using a novel reactor distributor, thereby improving reaction efficiency and reducing power consumption. Figure 1 As shown, the overall technical solution is as follows:

[0039] In reactor 1, a vertical distributor 2 and a ring distributor 3 are installed.

[0040] The annular distributor 3 is located on the central axis of the reactor 1. The annular distributor 3 includes a second air outlet 31 that opens upwards, which sprays air upwards during use.

[0041] The vertical distributor 2 is disposed between the annular distributor 3 and the inner wall of the reactor 1. The vertical distributor 2 includes a horizontally arranged first air outlet 21, which sprays air in the horizontal direction during use to form a vortex in the horizontal direction.

[0042] like Figure 2 As shown, the number of vertical distributors 2 can be set to multiple as needed. When there are multiple vertical distributors 2, they are evenly distributed around the ring distributor 3.

[0043] like Figure 3 As shown, the vertical distributor 2 includes a first air inlet flange 22 located below the bottom of the reactor 1, and a first bolt hole 23 is provided on the first air inlet flange 22. In use, the vertical distributor 2 is installed and connected to an external air supply device through the first air inlet flange 22 and the first bolt hole 23.

[0044] A vertical main pipe 24 is fixed above the first air inlet connection flange 22. The vertical main pipe 24 is a hollow cylindrical structure with an opening at the bottom that is fixedly connected to the first air inlet connection flange 22. It is vertically inserted into the reactor 1 and closed at the top.

[0045] The vertical main pipe 24 is located inside the reactor 1 and has a first gas outlet 21.

[0046] like Figure 4 As shown, the first air outlet 21 is opened outward along the tangent direction of the outer wall of the vertical main pipe 24.

[0047] The first air outlet 21 has multiple outlets on the same horizontal plane.

[0048] The first air outlet 21 is one layer on the same horizontal plane, and multiple layers can be opened as needed.

[0049] The first air outlet 21 is square.

[0050] like Figure 5 As shown, the annular distributor 3 includes an air inlet main pipe 35 extending out of the outer wall of the reactor 1. In use, the air inlet main pipe 35 is connected to an external air supply device to supply air to the annular distributor 3.

[0051] The main air inlet pipe 35 is located at one end inside the reactor 1 and is connected to the bottom end of the vertically connected pipe 36, which is set vertically upward.

[0052] A distribution ring 34 is horizontally arranged outside the vertical connecting pipe 36, and the distribution ring 34 is connected to the vertical connecting pipe 36 through a horizontally arranged horizontal connecting pipe 37.

[0053] The horizontal connecting pipe 37 can be set in multiple ways as needed, and when multiple are set, they are evenly distributed between the vertical connecting pipe 36 and the distribution ring 34.

[0054] The distribution ring 34 can be configured as a multi-layer structure as needed.

[0055] like Figure 6 As shown, the main air inlet pipe 35 is located at one end outside the reactor 1, and a second air inlet connecting flange 32 is fixedly provided. The second air inlet connecting flange 32 is provided with a second bolt hole 33. The annular distributor 3 is installed and connected to the external air supply device through the second air inlet connecting flange 32 and the second bolt hole 33.

[0056] like Figure 7 As shown, the distribution ring 34 is provided with a second air outlet 31, which is vertically upward.

[0057] The second air outlet 31 is circular.

[0058] Example:

[0059] This invention simultaneously installs a vertical distributor 2 and a ring distributor 3 inside the reactor 1. The two distributors are used in combination to achieve uniform distribution and thorough mixing.

[0060] The vertical distributor 2 is uniformly provided with square air outlets 21 (multiple vertical layers, and multiple air outlets set along the air inlet pipe in the horizontal direction). The air outlets are square and have a large area. Under pressure, they form a tangential force, which can drive the liquid phase to rotate and achieve the purpose of thorough stirring.

[0061] The annular distributor 3 has two layers of distribution rings 34, each with a circular vent 31 at its top. Under the pressure of the gas phase, an upward force is generated, driving the liquid upward and increasing the thoroughness of mixing. The two layers of distribution rings 34 are vertically aligned. Both layers of distribution rings 34 are connected to a vertical connecting pipe 33 by three horizontal connecting pipes 32. One end of each of the three horizontal connecting pipes 32 intersects and connects to the vertical connecting pipe 33, while the other end connects to the distribution ring 34.

[0062] In addition, the number of vertical distributors 2 can be increased or decreased depending on the viscosity and flowability of the liquid phase in reactor 1.

[0063] The number of layers of the annular distributor 34 can be increased or decreased according to the viscosity and flowability of the liquid phase in the reactor 1.

[0064] In addition to solid-liquid reactions, reactor 1 can also be used for liquid-liquid reactions.

[0065] This invention provides a novel reactor concept and method for achieving efficient feed distribution. Many methods and approaches exist for implementing this technical solution; the above description is merely a preferred embodiment. It should be noted that those skilled in the art can make various improvements and modifications without departing from the principles of this invention, and these improvements and modifications should also be considered within the scope of protection of this invention. All components not explicitly stated in this embodiment can be implemented using existing technology.

Claims

1. A novel reactor capable of achieving efficient feed distribution, characterized in that, include: A vertical distributor (2) and a ring distributor (3) are installed in the reactor (1); wherein, The annular distributor (3) is located on the central axis inside the reactor (1), and the annular distributor (3) is provided with a second air outlet (31) that is opened vertically upward. The vertical distributor (2) is disposed between the annular distributor (3) and the inner wall of the reactor (1), and the vertical distributor (2) is provided with a first horizontally opened air outlet (21).

2. The novel reactor according to claim 1, characterized in that, The number of vertical distributors (2) is one or more. When the number of vertical distributors (2) is two or more, the vertical distributors (2) are evenly distributed around the annular distributor (3).

3. A novel reactor capable of achieving efficient feed distribution according to claim 2, characterized in that, The vertical distributor (2) includes: A first air inlet connection flange (22) is provided below the bottom of the reactor (1), and a first bolt hole (23) is provided on the first air inlet connection flange (22) for installation and connection with an external air supply device; A vertical main pipe (24) is fixed above the first air inlet connecting flange (22). The vertical main pipe (24) is a hollow cylindrical structure. The bottom opening of the vertical main pipe (24) is fixedly connected to the top of the first air inlet connecting flange (22). The upper part of the vertical main pipe (24) is vertically inserted into the reactor (1). The top of the vertical main pipe (24) is closed. The vertical main pipe (24) is located inside the reactor (1) and has a first air outlet (21).

4. A novel reactor capable of achieving efficient feed distribution according to claim 3, characterized in that, The first air outlet (21) is opened outward along the tangential direction of the outer side wall of the vertical main pipe (24).

5. A novel reactor capable of achieving efficient feed distribution according to claim 4, characterized in that, The first air outlet (21) has multiple openings, among which the first air outlet (21) on the same horizontal plane is a single layer.

6. A novel reactor capable of achieving efficient feed distribution according to claim 5, characterized in that, The first air outlet (21) is configured to be multi-layered.

7. A novel reactor capable of achieving efficient feed distribution according to claim 6, characterized in that, The ring distributor (3) includes: A main air inlet pipe (35) extends horizontally out of the outer wall of the reactor (1). One end of the main air inlet pipe (35) is located inside the reactor (1) and is connected to the bottom end of a vertically arranged vertical connecting pipe (36). A distribution ring (34) is horizontally arranged on the outside of the vertical connecting pipe (36). The distribution ring (34) is connected to the vertical connecting pipe (36) through a horizontally arranged horizontal connecting pipe (37). The second air outlet (31) is opened on the distribution ring (34) and the opening direction is vertically upward.

8. A novel reactor capable of achieving efficient feed distribution according to claim 7, characterized in that, The horizontal connecting pipes (37) are configured in multiple ways and are evenly distributed between the vertical connecting pipes (36) and the distribution rings (34); the distribution rings (34) are configured in multiple layers.

9. A novel reactor capable of achieving efficient feed distribution according to claim 8, characterized in that, The main air inlet pipe (35) is located at one end outside the reactor (1), and a second air inlet connection flange (32) is fixedly provided thereon. The second air inlet connection flange (32) is provided with a second bolt hole (33) for installation and connection with an external air supply device.

10. A novel reactor capable of achieving efficient feed distribution according to claim 9, characterized in that, The first air outlet (21) is square; the second air outlet (31) is circular.

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