CN215939993U - High-efficient pipeline formula gathers expands type continuous mixing reactor - Google Patents
High-efficient pipeline formula gathers expands type continuous mixing reactor Download PDFInfo
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- CN215939993U CN215939993U CN202121911492.1U CN202121911492U CN215939993U CN 215939993 U CN215939993 U CN 215939993U CN 202121911492 U CN202121911492 U CN 202121911492U CN 215939993 U CN215939993 U CN 215939993U
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Abstract
The utility model discloses a high-efficiency pipeline type poly-expansion continuous mixing reactor, which comprises a tubular mixing unit, wherein a collecting pipe unit and a dispersing pipe unit are arranged in the mixing unit; the collecting pipe unit comprises a collecting baffle plate and a collecting pipe, the collecting pipe is arranged in the shaft center part of the mixing unit, and the collecting baffle plate is used for separating other areas of the cross section of the mixing unit; the dispersion pipe unit comprises dispersion pipes and a dispersion baffle plate, the dispersion pipes are arranged on the outer side of the dispersion baffle plate, and the dispersion baffle plate cuts off other areas of the cross section of the mixing unit; and the plurality of sections of the collecting pipe units and the dispersing pipe units are sequentially arranged in the mixing unit at intervals. The utility model can realize the full mixing of liquid phase raw materials.
Description
Technical Field
The utility model relates to a high-efficiency pipeline type poly-expansion type continuous mixing reactor used in the field of chemical industry.
Background
In the chemical industry field, in order to make the raw materials of the liquid phase fully react with each other and obtain a better reaction effect, the raw materials of the liquid phase need to be uniformly mixed, so that the molecules of the liquid phase are fully contacted. The existing reactor is mainly in a form of direct mixing or stirring mixing, so that more ideal mixing effect is difficult to obtain, and the reaction speed and the reaction effect are influenced.
SUMMERY OF THE UTILITY MODEL
The utility model aims to overcome the defects of the prior art and provide a high-efficiency pipeline type poly-expansion type continuous mixing reactor which can realize the full mixing of liquid phase raw materials.
One technical scheme for achieving the above purpose is as follows: a high-efficiency pipeline type poly-expanding continuous mixing reactor comprises a tubular mixing unit;
a collecting pipe unit and a dispersing pipe unit are arranged in the mixing unit; the collecting pipe unit comprises a collecting baffle plate and a collecting pipe, the collecting pipe is arranged in the shaft center part of the mixing unit, and the collecting baffle plate is used for separating other areas of the cross section of the mixing unit; the dispersion pipe unit comprises dispersion pipes and a dispersion baffle plate, the dispersion pipes are arranged on the outer side of the dispersion baffle plate, and the dispersion baffle plate cuts off other areas of the cross section of the mixing unit; and the plurality of sections of the collecting pipe units and the dispersing pipe units are sequentially arranged in the mixing unit at intervals.
Further, the diameter of the dispersion tube is smaller than the diameter of the collection tube.
Furthermore, a plurality of collecting pipes are arranged in the center of the collecting pipe unit, and a plurality of circles of dispersing pipes are arranged on the dispersing pipe unit.
Furthermore, a plurality of mixing units are connected in sequence to form a mixing unit group.
Furthermore, the inlet of the mixing unit group is connected with a multi-way joint through a flange, and the outlet of the mixing unit group is connected with an outlet connecting pipe through a flange.
By adopting the high-efficiency pipeline type poly-expansion continuous mixing reactor, the collecting pipe unit and the dispersing pipe unit are arranged in the mixing unit at intervals, and after various reaction solutions are introduced into the mixing unit, the reaction solutions are sequentially diffused when passing through the dispersing pipe unit, are blocked by the blocking plate and are collected when passing through the collecting pipe, so that the solutions of all phases can be continuously subjected to radial mixing action in the process of traveling along the mixing unit, full mixing is realized, the mixing effect is good, and the reaction quality is improved; can be according to the reaction needs with a plurality of mixing units with connect gradually and form continuous mixing reactor, prolonged the transport route of feed liquid, and then prolonged mix and reaction process, further promoted the reaction effect.
Drawings
FIG. 1 is a schematic structural diagram of a high-efficiency tubular poly-expansion type continuous mixing reactor according to the present invention;
FIG. 2 is a schematic structural diagram of a manifold unit of a high-efficiency tubular polymerization-expansion type continuous mixing reactor according to the present invention;
FIG. 3 is a schematic structural diagram of a dispersion pipe unit of a high-efficiency tubular poly-diffusion continuous mixing reactor according to the present invention.
Detailed Description
In order to better understand the technical solution of the present invention, the following detailed description is made by specific examples:
referring to fig. 1 to 3, a high-efficiency pipeline type polymerization-expansion type continuous mixing reactor according to the present invention is composed of tubular mixing units connected in sequence. The mixing unit is internally provided with a collecting pipe unit and a dispersing pipe unit.
Referring to fig. 2, the manifold unit includes a manifold baffle 9 and a manifold 10. The collecting pipe 10 is arranged at the axial center part of the mixing unit, and the collecting baffle plate 9 is used for separating other areas of the cross section of the mixing unit. In this embodiment, one manifold 10 is provided, and a plurality of manifolds may be designed as required in practical application.
Referring to fig. 3, the dispersion pipe unit includes a dispersion pipe 7 and a dispersion blocking plate 8. The dispersion pipes 7 are arranged outside the dispersion blocking plate, and the diameter of each dispersion pipe 7 is smaller than that of the collection pipe 10. The dispersion baffle 8 cuts off the other regions of the cross section of the mixing unit. A circle of dispersion pipes 7 are arranged in the embodiment, and multiple circles of dispersion pipes can be designed according to needs in practical application.
The plurality of sections of the collecting pipe units and the dispersing pipe units are sequentially arranged in the mixing unit at intervals. A plurality of mixing units are connected in sequence through communicating flanges 13 and communicating pipes 14 to form a mixing unit group, and the mixing unit group is supported through a support frame 12. The inlet of the mixing unit group is connected with a multi-way joint through a flange and is used for accessing different types of feed liquid; the outlet of the mixing unit group is connected with a connecting pipe 2 through an outlet flange 4 and an outlet flange cover 3, and the connecting pipe 2 is connected with a blanking flange 1.
It should be understood by those skilled in the art that the above embodiments are only for illustrating the present invention and are not to be used as a limitation of the present invention, and that changes and modifications to the above described embodiments are within the scope of the claims of the present invention as long as they are within the spirit and scope of the present invention.
Claims (5)
1. The utility model provides a high-efficient pipeline formula gathers expands type continuous mixing reactor, includes the tubulose mixing unit, its characterized in that:
a collecting pipe unit and a dispersing pipe unit are arranged in the mixing unit; the collecting pipe unit comprises a collecting baffle plate and a collecting pipe, the collecting pipe is arranged in the shaft center part of the mixing unit, and the collecting baffle plate is used for separating other areas of the cross section of the mixing unit; the dispersion pipe unit comprises dispersion pipes and a dispersion baffle plate, the dispersion pipes are arranged on the outer side of the dispersion baffle plate, and the dispersion baffle plate cuts off other areas of the cross section of the mixing unit; and the plurality of sections of the collecting pipe units and the dispersing pipe units are sequentially arranged in the mixing unit at intervals.
2. A high efficiency tubular poly-amplification continuous mixing reactor as claimed in claim 1, wherein the diameter of the dispersion tube is smaller than the diameter of the collection tube.
3. The high efficiency tubular polymerization-expansion type continuous mixing reactor according to claim 1, wherein a plurality of collecting tubes are provided at the center of the collecting tube unit, and a plurality of circles of dispersing tubes are provided on the dispersing tube unit.
4. The efficient pipeline type poly-expansion continuous mixing reactor according to claim 1, wherein a plurality of mixing units are connected in sequence to form a mixing unit group.
5. A high-efficiency pipeline type poly-expansion continuous mixing reactor as claimed in claim 4, wherein the inlet of the mixing unit set is connected with a multi-way joint through a flange, and the outlet of the mixing unit set is connected with an outlet connecting pipe through a flange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121911492.1U CN215939993U (en) | 2021-08-16 | 2021-08-16 | High-efficient pipeline formula gathers expands type continuous mixing reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121911492.1U CN215939993U (en) | 2021-08-16 | 2021-08-16 | High-efficient pipeline formula gathers expands type continuous mixing reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215939993U true CN215939993U (en) | 2022-03-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121911492.1U Active CN215939993U (en) | 2021-08-16 | 2021-08-16 | High-efficient pipeline formula gathers expands type continuous mixing reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215939993U (en) |
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2021
- 2021-08-16 CN CN202121911492.1U patent/CN215939993U/en active Active
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