CN215611626U - Continuous dipping device of 2-methylpyrazine synthetic process catalyst - Google Patents
Continuous dipping device of 2-methylpyrazine synthetic process catalyst Download PDFInfo
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- CN215611626U CN215611626U CN202121705653.1U CN202121705653U CN215611626U CN 215611626 U CN215611626 U CN 215611626U CN 202121705653 U CN202121705653 U CN 202121705653U CN 215611626 U CN215611626 U CN 215611626U
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Abstract
The utility model discloses a continuous catalyst impregnation device in a 2-methylpyrazine synthesis process, which comprises a shell, wherein a transverse pipe is welded on the outer wall of the top of the shell, an inclined pipe is welded at one end of the transverse pipe, a first rotating shaft is arranged inside the transverse pipe, a second rotating shaft is arranged inside the inclined pipe, a universal joint is connected between the first rotating shaft and the second rotating shaft through a pin, a connecting pipe is welded on the outer wall of the bottom of the inclined pipe, the bottom end of the connecting pipe is welded with the shell, a box body is welded on the outer wall of one side of the shell, uniformly distributed heating wires are arranged inside the box body, a main pipe is connected to the outer wall of one side of the shell through bolts, a branch pipe is welded between the main pipe and the shell, and one end of the main pipe is welded with the box body. According to the utility model, the carrier solution is filled in the transverse pipe, so that the first rotating shaft and the second rotating shaft are used for driving the auger plate to rotate, the carrier can be continuously impregnated in the active solution, and the effect of high catalyst impregnation efficiency is further realized.
Description
Technical Field
The utility model relates to the technical field of 2-methylpyrazine production, in particular to a continuous catalyst impregnation device in a 2-methylpyrazine synthesis process.
Background
2-methyl pyrazine, a chemical substance, is often used as a food additive, a catalyst is needed in the synthesis process of 2-methyl pyrazine, a carrier using the catalyst is immersed in an active solution, and then the inside of the carrier is provided with active ingredients in the active solution.
When the catalyst is subjected to dipping processing in the 2-methylpyrazine synthesis process in the prior art, the carrier cannot be continuously dipped, so that the dipping efficiency of the catalyst is reduced, and the catalyst is required to be moved to another device for drying after being dipped, so that the production of the catalyst is troublesome. Therefore, it is necessary to design a continuous catalyst impregnation device for 2-methylpyrazine synthesis to solve the above problems.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the defects of low impregnation efficiency and troublesome production process in the prior art, and provides a continuous catalyst impregnation device for a 2-methylpyrazine synthesis process.
In order to achieve the purpose, the utility model adopts the following technical scheme: the utility model provides a 2-methylpyrazine synthetic process catalyst impregnating device in succession, includes the casing, the welding of the top outer wall of casing has violently the pipe, the one end welding of violently managing has the pipe chute, the inside of violently managing is provided with first pivot, the inside of pipe chute is provided with the second pivot, there is the universal joint through the round pin columnar connection between first pivot and the second pivot, the welding of the bottom outer wall of pipe chute has the connecting pipe, the bottom and the casing welding of connecting pipe, one side outer wall welding of casing has the box, the inside of box is provided with evenly distributed's heater strip, one side outer wall of casing has the person in charge through bolted connection, the welding has the branch pipe between person in charge and the casing, the one end and the box welding of being responsible for.
The key concept of the technical scheme is as follows: the carrier solution is filled in the horizontal pipe by utilizing the first rotating shaft and the second rotating shaft to drive the auger plate to rotate, so that the carrier can be continuously impregnated in the active solution, and the effect of high catalyst impregnation efficiency is realized.
Furthermore, the outer wall of one side of the transverse pipe is connected with a motor through a bolt, and one end of an output shaft of the motor is connected with the first rotating shaft through a spline.
Furthermore, an inclined plate is welded between the inner walls of the two sides of the shell, and micropores which are uniformly distributed are formed in the outer wall of the top of the inclined plate.
Furthermore, the outer wall of one side of the shell is connected with an air blower through a bolt, and an air outlet pipe of the air blower is connected with the box body through a bolt.
Furthermore, an air outlet pipe is welded on the outer wall of the top of the shell, and a blocking net is arranged at the top of the air outlet pipe.
Furthermore, the top outer wall welding of violently managing has the feeder hopper, one side outer wall welding of casing has out the hopper.
Furthermore, four supporting legs are welded on the outer wall of the bottom of the shell, and reinforcing plates are welded between every two adjacent supporting legs.
The utility model has the beneficial effects that:
1. through the first pivot, the second pivot and the hank dragon board that set up, utilize to fill carrier solution in the inside of violently managing for utilize first pivot and second pivot to drive the hank dragon board and rotate, can realize that the carrier carries out continuous flooding inside active solution, and then realized the efficient effect of catalyst flooding.
2. Through the heater strip and the air-blower that set up, utilize the heater strip to heat the inside air of box, the rethread air-blower blows in steam the casing inside and carries out the drying to the carrier, and then makes the flooding and the drying of catalyst can accomplish inside same equipment for the production convenience more of catalyst.
3. Through the swash plate and the micropore that set up, can fluidize the carrier when utilizing steam to pass the micropore of swash plate for the drying efficiency of carrier is faster, and can flow to a hopper department through the swash plate smoothly, has consequently further realized the convenient effect of catalyst processing.
4. Through the outlet duct and the arresting net that set up, utilize the outlet duct to make the inside moist air of casing be convenient for discharge the casing, utilize the arresting net to prevent that the catalyst of fluidization from discharging from the outlet duct, and then reduced the waste that the catalyst produced in process of production.
Drawings
FIG. 1 is a schematic view of the overall structure of a continuous catalyst impregnation device for 2-methylpyrazine synthesis according to the present invention;
FIG. 2 is a schematic view of the internal structure of a continuous catalyst impregnation device for 2-methylpyrazine synthesis according to the present invention;
FIG. 3 is a schematic diagram of a packing auger plate structure of a continuous catalyst impregnation device for 2-methylpyrazine synthesis according to the present invention.
In the figure: the device comprises a shell 1, a horizontal pipe 2, a feed hopper 3, an air outlet pipe 4, an inclined pipe 5, a connecting pipe 6, a box 7, an air blower 8, a main pipe 9, support legs 10, a reinforcing plate 11, branch pipes 12, a blocking net 13, a discharge hopper 14, a first rotating shaft 15, a second rotating shaft 16, a twisted dragon plate 17, a universal joint 18, a motor 19, an inclined plate 20, micropores 21 and heating wires 22.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1 to 3, a continuous catalyst impregnation device for a 2-methylpyrazine synthesis process includes a housing 1, a horizontal pipe 2 welded to an outer wall of a top of the housing 1, an inclined pipe 5 welded to one end of the horizontal pipe 2 for containing an active solution, a first rotating shaft 15 arranged inside the horizontal pipe 2, a second rotating shaft 16 arranged inside the inclined pipe 5, a universal joint 18 connected between the first rotating shaft 15 and the second rotating shaft 16 through a pin, a connecting pipe 6 welded to an outer wall of a bottom of the inclined pipe 5, a bottom end of the connecting pipe 6 welded to the housing 1, a box 7 welded to an outer wall of one side of the housing 1, uniformly distributed heating wires 22 arranged inside the box 7, heating heat by the heating wires 22, a main pipe 9 connected to an outer wall of one side of the housing 1 through a bolt, a branch pipe 12 welded between the main pipe 9 and the housing 1, and one end of the main pipe 9 welded to the box 7, so that heat can enter the interior of the housing 1 through the main pipe 9 and the branch pipes 12.
As apparent from the above description, the present invention has the following advantageous effects: through the first pivot 15, the second pivot 16 and the auger plate 17 that set up, utilize and fill carrier solution in violently managing 2 inside for utilize first pivot 15 and the 16 drive auger plate 17 of second pivot to rotate, can realize that the carrier carries out continuous flooding inside active solution, and then realized the efficient effect of catalyst flooding.
Further, the outer wall of one side of the transverse tube 2 is connected with an electric motor 19 through a bolt, the model of the electric motor 19 is CH-28, one end of an output shaft of the electric motor 19 is connected with the first rotating shaft 15 through a spline, and the electric motor 19 drives the first rotating shaft 15 to rotate.
Furthermore, an inclined plate 20 is welded between the inner walls of the two sides of the shell 1, the outer wall of the top of the inclined plate 20 is provided with uniformly distributed micropores 21, and the micropores 21 are utilized to fluidize the carrier on the inclined plate 20 when gas passes through the micropores 21.
Further, the outer wall of one side of the shell 1 is connected with a blower 8 through a bolt, the model of the blower 8 is CZ-TD550, an air outlet pipe of the blower 8 is connected with the box 7 through a bolt, and hot air in the box 7 is blown into the shell 1 through the blower 8, so that the hot air dries the catalyst.
Furthermore, an air outlet pipe 4 is welded on the outer wall of the top of the shell 1, a blocking net 13 is arranged on the top of the air outlet pipe 4, and fluidized catalyst is prevented from being blown out of the shell 1 by the blocking net 13.
Further, the welding of the top outer wall of violently managing 2 has feeder hopper 3, through feeder hopper 3 to violently managing 2 inside joining carriers, the welding of one side outer wall of casing 1 has out hopper 14, and the catalyst after the drying flows from out hopper 14.
Furthermore, four supporting legs 10 are welded on the outer wall of the bottom of the shell 1, reinforcing plates 11 are welded between two adjacent supporting legs 10, and the supporting legs 10 are reinforced by the reinforcing plates 11.
Adopt foretell heater strip 22 and air-blower 8, utilize heater strip 22 to heat the inside air of box 7, rethread air-blower 8 blows in casing 1 inside to the carrier drying to steam, and then makes the flooding and the drying of catalyst can accomplish inside same equipment for the production of catalyst is more convenient.
Some preferred embodiments or application examples are listed below to help those skilled in the art to better understand the technical content of the present invention and the technical contribution of the present invention with respect to the prior art:
example 1
A catalyst continuous impregnation device in a 2-methylpyrazine synthesis process comprises a shell 1, a horizontal pipe 2 is welded on the outer wall of the top of the shell 1, an inclined pipe 5 is welded at one end of the horizontal pipe 2, can utilize violently pipe 2 splendid attire active solution, the inside of violently pipe 2 is provided with first pivot 15, the inside of pipe chute 5 is provided with second pivot 16, there is universal joint 18 through the round pin post connection between first pivot 15 and the second pivot 16, the bottom outer wall welding of pipe chute 5 has connecting pipe 6, the bottom and the welding of casing 1 of connecting pipe 6, one side outer wall welding of casing 1 has box 7, the inside of box 7 is provided with evenly distributed's heater strip 22, utilize heater strip 22 circular telegram to provide the heat, one side outer wall of casing 1 has the person in charge 9 through bolted connection, the welding has branch pipe 12 between being responsible for 9 and the casing 1, the one end and the welding of box 7 of being responsible for 9, make the heat can get into inside the casing 1 through being responsible for 9 and branch pipe 12.
The outer wall of one side of the transverse pipe 2 is connected with a motor 19 through a bolt, the model of the motor 19 is CH-28, one end of an output shaft of the motor 19 is connected with the first rotating shaft 15 through a spline, and the motor 19 is used for driving the first rotating shaft 15 to rotate; an inclined plate 20 is welded between the inner walls of the two sides of the shell 1, the outer wall of the top of the inclined plate 20 is provided with uniformly distributed micropores 21, and the micropores 21 are utilized to fluidize a carrier on the inclined plate 20 when gas passes through the micropores 21; the outer wall of one side of the shell 1 is connected with a blower 8 through a bolt, the model of the blower 8 is CZ-TD550, an air outlet pipe of the blower 8 is connected with the box body 7 through a bolt, and hot air in the box body 7 is blown into the shell 1 through the blower 8, so that the hot air dries the catalyst; an air outlet pipe 4 is welded on the outer wall of the top of the shell 1, a blocking net 13 is arranged on the top of the air outlet pipe 4, and fluidized catalyst is prevented from being blown out of the shell 1 by the blocking net 13; the outer wall of the top of the transverse pipe 2 is welded with a feed hopper 3, a carrier is added into the transverse pipe 2 through the feed hopper 3, the outer wall of one side of the shell 1 is welded with a discharge hopper 14, and dried catalyst flows out of the discharge hopper 14; four landing legs 10 are welded to the outer wall of the bottom of the shell 1, reinforcing plates 11 are welded between every two adjacent landing legs 10, and the landing legs 10 are reinforced through the reinforcing plates 11.
The working principle is as follows: when the catalyst carrier is used, when the catalyst carrier needs to be impregnated, an active solution is added into the horizontal pipe 2 through the feed hopper 3, the liquid level of the active solution is enabled to be flush with the inner wall of the top of the horizontal pipe 2, the power supply of the motor 19, the heating wire 22 and the blower 8 is connected through a lead, the carrier is continuously added into the horizontal pipe 2 through the feed hopper 3, the motor 19 drives the first rotating shaft 15 to rotate when in work, the first rotating shaft 15 drives the second rotating shaft 16 to rotate through the universal joint 18, and further the carrier is conveyed and continuously impregnated by the auger plates 17 outside the first rotating shaft 15 and the second rotating shaft 16, so that the carrier sequentially enters the shell 1 from the inside of the horizontal pipe 2 through the inclined pipe 5 and the connecting pipe 6, and falls on the inclined plate 20, and when the blower 8 and the heating wire 22 work, the heating wire 22 heats the inside of the box body 7, the blower 8 blows hot air into the bottom of the inclined plate 20 through the main pipe 9 and the branch pipes 12, the hot air fluidizes the carrier when passing through the micropores 21 of the inclined plate 20 and flows to the side of the discharge hopper 14 on the inclined plate 20, and the hot air dries the wet carrier to form a catalyst and flows out of the discharge hopper 14.
The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be considered to be within the technical scope of the present invention, and equivalent alternatives or modifications according to the technical solution of the present invention and the inventive concept thereof should be covered by the scope of the present invention.
Claims (7)
1. The utility model provides a 2-methylpyrazine synthetic process catalyst continuous impregnation device, includes casing (1), its characterized in that, the welding of the top outer wall of casing (1) has violently the pipe (2), the welding of the one end of violently managing (2) has pipe chute (5), the inside of violently managing (2) is provided with first pivot (15), the inside of pipe chute (5) is provided with second pivot (16), be connected with universal joint (18) through the round pin post between first pivot (15) and second pivot (16), the welding of the bottom outer wall of pipe chute (5) has connecting pipe (6), the bottom and the welding of casing (1) of connecting pipe (6), the welding of one side outer wall of casing (1) has box (7), the inside of box (7) is provided with evenly distributed's heater strip (22), there is the person in charge (9) one side outer wall of casing (1) through bolted connection, a branch pipe (12) is welded between the main pipe (9) and the shell (1), and one end of the main pipe (9) is welded with the box body (7).
2. The continuous catalyst impregnation device for the 2-methylpyrazine synthesis process according to claim 1, wherein an outer wall of one side of the horizontal tube (2) is connected with an electric motor (19) through a bolt, and one end of an output shaft of the electric motor (19) is connected with the first rotating shaft (15) through a spline.
3. The continuous catalyst impregnation device for the 2-methylpyrazine synthesis process according to claim 1, characterized in that an inclined plate (20) is welded between the inner walls of the two sides of the casing (1), and the outer wall of the top of the inclined plate (20) is provided with uniformly distributed micropores (21).
4. The continuous catalyst impregnation device for the 2-methylpyrazine synthesis process according to claim 1, wherein an air blower (8) is connected to the outer wall of one side of the casing (1) through a bolt, and an air outlet pipe of the air blower (8) is connected to the box body (7) through a bolt.
5. The continuous catalyst impregnation device for the 2-methylpyrazine synthesis process according to claim 1, characterized in that an outlet pipe (4) is welded to the outer wall of the top of the shell (1), and a barrier net (13) is arranged on the top of the outlet pipe (4).
6. The continuous catalyst impregnation device for the 2-methylpyrazine synthesis process according to claim 1, characterized in that a feed hopper (3) is welded to the outer wall of the top of the horizontal tube (2), and a discharge hopper (14) is welded to the outer wall of one side of the shell (1).
7. The continuous catalyst impregnation device for the 2-methylpyrazine synthesis process according to claim 1, characterized in that four legs (10) are welded to the outer wall of the bottom of the casing (1), and a reinforcing plate (11) is welded between two adjacent legs (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121705653.1U CN215611626U (en) | 2021-07-26 | 2021-07-26 | Continuous dipping device of 2-methylpyrazine synthetic process catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121705653.1U CN215611626U (en) | 2021-07-26 | 2021-07-26 | Continuous dipping device of 2-methylpyrazine synthetic process catalyst |
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| Publication Number | Publication Date |
|---|---|
| CN215611626U true CN215611626U (en) | 2022-01-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121705653.1U Active CN215611626U (en) | 2021-07-26 | 2021-07-26 | Continuous dipping device of 2-methylpyrazine synthetic process catalyst |
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| CN (1) | CN215611626U (en) |
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- 2021-07-26 CN CN202121705653.1U patent/CN215611626U/en active Active
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