Microporous vortex plate type reactor

Abstract

The utility model discloses a micropore vortex plate type reactor which comprises a shell, an air inlet and an air outlet are respectively arranged at the top end and the bottom end of the shell, a support rod is fixedly arranged in the air inlet, a cover plate is covered on the air inlet, a first air guide mechanism and a second air guide mechanism which have the same structure are arranged in the shell, and the first air guide mechanism and the second air guide mechanism are fixedly arranged on the support rod. Two different gases are released in a shell through a first gas guide mechanism and a second gas guide mechanism and disturbed, the first gas guide mechanism comprises a first gas inlet pipeline, and the first gas inlet pipeline penetrates through a supporting rod and is fixedly connected with the supporting rod. Through the arrangement of the first gas guide mechanism and the second gas guide mechanism, two kinds of reaction gas can be uniformly dispersed and released in the shell, and the two kinds of gas generate vortex along with the rotation of the first splitter plate and the second splitter plate, so that the gas is mixed more sufficiently, and the reaction is more sufficient.

Description

Technical Field

[0001] The utility model relates to the technical field of reactors, in particular to a microporous vortex plate reactor. Background Art

[0002] The Chinese utility model patent with publication number CN215996680U discloses a shell, wherein an inner cylinder is provided at the center of the interior of the shell, and a plurality of plate pairs are evenly provided on the outer wall of the inner cylinder, each group of the plate pairs includes two corrugated plates, a sealing plate is fixedly connected between the two corrugated plates, and a heat exchange cavity is formed between the two corrugated plates, the sealing plate and the inner cylinder; a coolant flows through the interior of the corrugated plates, a catalyst is contained in the interior of the heat exchange cavity and a reaction gas flows; the ends of the plurality of plate pairs are fixedly mounted on the inner wall of the shell; the corrugated plates are of a bubbling type; a lower boss is fixedly mounted on the bottom of the shell, an air outlet is provided at the bottom of the lower boss, and the air outlet is used to discharge the reaction gas; a coolant distribution pipe is provided on the inner wall of the lower boss, and the top of the coolant distribution pipe is interconnected with the corrugated plates. The outer wall of the shell is also connected with a cooling liquid inlet pipe, and the end of the cooling liquid inlet pipe passes through the lower boss and extends to the outside of the lower boss; the top of the shell is fixedly mounted with an upper boss, and the top of the upper boss is provided with an air inlet, and the air inlet is used to pass the reaction gas; the bottom of the steam collecting pipe and the corrugated plate are mutually penetrated, and the outer wall of the steam collecting pipe is also connected with a steam outlet pipe, and the end of the steam outlet pipe passes through the upper boss and extends to the outside of the upper boss; a rotary gas distributor is also provided inside the upper boss, and the rotary gas distributor is used to evenly disperse the reaction gas introduced from the air inlet; the rotary gas distributor includes a fixing frame, a bearing and a fan, a bearing is provided at the center of the interior of the upper boss, and a fan is rotatably provided at the bottom of the bearing, a fixing frame is fixedly mounted on the outer wall of the bearing, and the end of the fixing frame is fixedly mounted on the inner wall of the upper boss.

[0003] The above patent has the following deficiencies:

[0004] The corrugated plates are fixed, and the gas phase discharged through the corrugated plates has a fixed flow direction and cannot form a vortex, so it is difficult to fully mix different types of gas phase substances, resulting in incomplete reaction. Utility Model Content

[0005] In view of the problems existing in an existing microporous vortex plate reactor, the present utility model is proposed.

[0006] Therefore, the purpose of the present invention is to provide a microporous vortex plate reactor, which solves the problem in the above-mentioned patent that the corrugated plate is fixed, the gas phase discharged through the corrugated plate flows in a fixed direction and cannot form a vortex, making it difficult to fully mix different types of gas phase substances, thereby leading to insufficient reaction.

[0007] In order to solve the above technical problems, according to one aspect of the present invention, the present invention provides the following technical solutions:

[0008] A microporous vortex plate reactor includes a shell, the top and bottom of the shell are respectively provided with an air inlet and an air outlet, a support rod is fixedly installed in the air inlet, and the air inlet is covered with a cover plate, and a first air guide mechanism and a second air guide mechanism with the same structure are provided in the shell, through which two different gases are released into the shell and the gases are disturbed.

[0009] As a preferred solution of a microporous vortex plate reactor described in the utility model, wherein: the first air guide mechanism includes a first air inlet pipe, the first air inlet pipe passes through the support rod and is fixedly connected between the support rod, the end of the first air inlet pipe is connected to the first gas dispersion and release pipe through a first rotary joint, the first gas dispersion and release pipe is evenly fixed with a first diversion plate, and the first diversion plate is equidistantly provided with first through holes connecting to the first gas dispersion and release pipe.

[0010] As a preferred solution of the microporous vortex plate reactor described in the present invention, wherein: the first gas dispersion and release pipeline is connected to a first driving mechanism;

[0011] The first driving mechanism includes a first support plate welded to the shell, a first motor is mounted on the first support plate, an output shaft of the first motor is fixedly connected to a first driving gear, the first driving gear is meshed with a first driven gear, and the first driven gear is fixedly mounted on a first gas dispersion and release pipe.

[0012] As a preferred solution of a microporous vortex plate reactor described in the utility model, wherein: the second air guide mechanism includes a second air inlet pipe, the second air inlet pipe passes through the support rod and is fixedly connected between the support rod, the end of the second air inlet pipe is connected to the second gas dispersion and release pipe through a second rotary joint, the second gas dispersion and release pipe is evenly fixed with a second diversion plate, and the first diversion plate is equidistantly provided with second through holes connecting to the second gas dispersion and release pipe.

[0013] As a preferred solution of the microporous vortex plate reactor described in the present invention, wherein: the second gas dispersion and release pipeline is connected to a second driving mechanism;

[0014] The first driving mechanism includes a second support plate welded to the shell, a second motor is mounted on the second support plate, an output shaft of the second motor is fixedly connected to a second driving gear, the second driving gear is meshedly connected to a second driven gear, and the second driven gear is fixedly mounted on the second gas dispersion and release pipeline.

[0015] As a preferred solution of the microporous vortex plate reactor described in the utility model, a support beam is fixedly installed in the air outlet, and a fan is fixedly installed on the support beam.

[0016] Compared with existing technologies:

[0017] By setting up the first gas guide mechanism and the second gas guide mechanism, the two reaction gases can be evenly distributed and released in the shell, and the two gases generate vortices as the first diverter plate and the second diverter plate rotate, so that the gases are mixed more fully, and thus the reaction will also be more complete. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] Figure 1 This is a schematic diagram of the structure of Example 1 of the present utility model;

[0019] Figure 2 Provided in Example 1 of the present utility model Figure 1 sectional view of

[0020] Figure 3 Provided in Example 1 of the present utility model Figure 2 Enlarged view of point A in the middle;

[0021] Figure 4 Provided in Example 1 of the present utility model Figure 2 Enlarged view of point B in the middle;

[0022] Figure 5 This is a cross-sectional view of the first gas dispersion and release pipeline provided in Example 1 of the present utility model.

[0023] In the figure: shell 1, air inlet 2, air outlet 3, fan 4, support beam 5, support rod 6, first air inlet duct 100, first gas dispersion and release duct 102, first diverter plate 103, first through hole 1031, first support plate 104, first motor 105, first driving gear 106, first driven gear 107, first rotary joint 108, second air inlet duct 200, second gas dispersion and release duct 202, second diverter plate 203, second through hole 2031, second support plate 204, second motor 205, second driving gear 206, second driven gear 207, second rotary joint 208, cover plate 7. DETAILED DESCRIPTION

[0024] In order to make the purpose, technical solutions and advantages of the present invention more clear, the embodiments of the present invention will be described in further detail below with reference to the accompanying drawings.

[0025] The utility model provides a microporous vortex plate reactor, please refer to Figure 1-5 , including a shell 1, the top and bottom ends of the shell 1 are respectively provided with an air inlet 2 and an air outlet 3, a support beam 5 is fixedly installed in the air outlet 3, and a fan 4 is fixedly installed on the support beam 5, and the fan 4 rotates to suck out the reacted gas in the shell 1, a support rod 6 is fixedly installed in the air inlet 2, and a cover plate 7 is covered on the air inlet 2, which is sealed between the cover plate 7 and the first air inlet duct 100 and the second air inlet duct 200, and a first air guide mechanism and a second air guide mechanism with the same structure are provided in the shell 1, and two different gases are released into the shell 1 through the first air guide mechanism and the second air guide mechanism and disturb the gas.

[0026] The first air guide mechanism includes a first air intake pipe 100, which passes through the support rod 6 and is fixedly connected to the support rod 6. The end of the first air intake pipe 100 is connected to the first gas dispersion and release pipe 102 through a first rotary joint 108. The first gas dispersion and release pipe 102 is evenly fixed with a first diverter plate 103, and the first diverter plate 103 is equidistantly provided with first through holes 1031 connecting to the first gas dispersion and release pipe 102; the top end of the first air intake pipe 100 extends out of the air inlet 2 and docks with the gas delivery pipe.

[0027] The first gas dispersion and release pipeline 102 is transmission-connected to a first driving mechanism; the first driving mechanism includes a first support plate 104 welded to the shell 1, a first motor 105 is mounted on the first support plate 104, the output shaft of the first motor 105 is fixedly connected to a first driving gear 106, the first driving gear 106 is meshedly connected to a first driven gear 107, and the first driven gear 107 is fixedly mounted on the first gas dispersion and release pipeline 102.

[0028] The second air guide mechanism includes a second air intake pipe 200, which passes through the support rod 6 and is fixedly connected to the support rod 6. The end of the second air intake pipe 200 is connected to the second gas dispersion and release pipe 202 via a second rotary joint 208. Second diverter plates 203 are evenly fixed on the second gas dispersion and release pipe 202. Second through holes 2031 that communicate with the second gas dispersion and release pipe 202 are evenly spaced on the second diverter plates 203. The top end of the second air intake pipe 200 extends out of the air inlet 2 and connects to the gas transmission pipe.

[0029] The second gas dispersion and release pipeline 202 is transmission-connected to the second driving mechanism; the first driving mechanism includes a second support plate 204 welded to the shell 1, and a second motor 205 is installed on the second support plate 204. The output shaft of the second motor 205 is fixedly connected to the second driving gear 206, and the second driving gear 206 is meshedly connected to the second driven gear 207. The second driven gear 207 is fixedly installed on the second gas dispersion and release pipeline 202; the first driving mechanism drives the second gas dispersion and release pipeline 202 and the pipeline thereon.

[0030] During specific use, the first air inlet pipe 100 and the second air inlet pipe 200 are respectively connected to the pipes for conveying the two reaction gases; the first motor 105 is started to drive the first gas dispersion and release pipe 102 to rotate, and the second motor 205 is started to drive the second gas dispersion and release pipe 202 to rotate. The two gases are respectively discharged through the first through hole 1031 on the first diverter plate 103 and the second through hole 2031 on the second diverter plate 203. After the two reaction gases are fully mixed and reacted, they are discharged through the outlet 3.

[0031] While the present invention has been described above with reference to specific embodiments, various modifications may be made and equivalent components may be substituted without departing from the scope of the present invention. In particular, as long as no structural conflicts exist, the various features of the embodiments disclosed herein may be combined with one another in any manner, and the omission of an exhaustive description of these combinations in this specification is solely for the sake of space and resource conservation. Therefore, the present invention is not limited to the specific embodiments disclosed herein, but encompasses all technical solutions within the scope of the claims.

Claims

1. A microporous vortex plate reactor, comprising a shell (1), wherein the top and bottom ends of the shell (1) are respectively provided with an air inlet (2) and an air outlet (3), a support rod (6) is fixedly installed in the air inlet (2), and a cover plate (7) is covered on the air inlet (2), characterized in that: A first gas guide mechanism and a second gas guide mechanism with the same structure are provided in the housing (1), and two different gases are released into the housing (1) through the first gas guide mechanism and the second gas guide mechanism, and the gases are disturbed.

2. A microporous vortex plate reactor according to claim 1, characterized in that: The first air guide mechanism comprises a first air intake pipe (100), the first air intake pipe (100) passes through a support rod (6) and is fixedly connected to the support rod (6), the end of the first air intake pipe (100) is connected to a first gas dispersion and release pipe (102) via a first rotary joint (108), a first diverter plate (103) is evenly fixed on the first gas dispersion and release pipe (102), and first through holes (1031) connected to the first gas dispersion and release pipe (102) are equidistantly provided on the first diverter plate (103).

3. A microporous vortex plate reactor according to claim 2, characterized in that: The first gas dispersion and release pipeline (102) is transmission-connected to a first driving mechanism; The first driving mechanism comprises a first support plate (104) welded to the housing (1); a first motor (105) is mounted on the first support plate (104); an output shaft of the first motor (105) is fixedly connected to a first driving gear (106); the first driving gear (106) is meshedly connected to a first driven gear (107); and the first driven gear (107) is fixedly mounted on a first gas dispersion and release pipe (102).

4. A microporous vortex plate reactor according to claim 3, characterized in that: The second air guide mechanism comprises a second air intake pipe (200), the second air intake pipe (200) passes through the support rod (6) and is fixedly connected to the support rod (6), the end of the second air intake pipe (200) is connected to the second gas dispersion and release pipe (202) via a second rotary joint (208), a second diverter plate (203) is evenly fixed on the second gas dispersion and release pipe (202), and second through holes (2031) connected to the second gas dispersion and release pipe (202) are equidistantly provided on the second diverter plate (203).

5. A microporous vortex plate reactor according to claim 4, characterized in that: The second gas dispersion and release pipeline (202) is transmission-connected to a second driving mechanism; The first driving mechanism comprises a second support plate (204) welded to the housing (1); a second motor (205) is mounted on the second support plate (204); an output shaft of the second motor (205) is fixedly connected to a second driving gear (206); the second driving gear (206) is meshedly connected to a second driven gear (207); and the second driven gear (207) is fixedly mounted on a second gas dispersion and release pipe (202).

6. A microporous vortex plate reactor according to claim 5, characterized in that: A support beam (5) is fixedly mounted in the air outlet (3), and a fan (4) is fixedly mounted on the support beam (5).

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