Continuous flow reactor for accelerating mixing

Abstract

The utility model discloses a continuous flow reactor for accelerating mixing, which relates to the technical field of continuous flow reactors and comprises a tower reactor, the tower reactor is formed by stacking a plurality of tower sections up and down, and a heat exchange jacket is arranged in the middle of each tower section. According to the continuous flow reactor capable of accelerating mixing, the tower type reactor is formed by vertically stacking the tower sections, the vertically adjacent tower sections are fixed through connecting flange bolts when the tower type reactor is used, and inner cavities of the vertically adjacent tower sections are communicated through cooperation of liquid lifting holes and guide pipes and cooperation of via holes and butt joint pipes; the tower-type structural design is small in occupied area, the volume utilization rate is increased, the number of building layers and the using number can be designed according to the actual situation, and the reactor can be used as a single-layer reactor or a multi-layer reactor, that is, one reactor can achieve the functions of multiple reactors, the reaction time is shortened, backmixing is reduced, and the efficiency is higher. And higher economic and teaching benefits can be brought.

Description

Technical Field

[0001] The utility model relates to the technical field of continuous flow reactors, in particular to a continuous flow reactor for accelerating mixing. Background Art

[0002] A continuous flow reactor is a device that continuously performs chemical reactions. During the reaction, reactants and solvents flow continuously and complete the chemical reaction process simultaneously.

[0003] However, traditional kettle-type continuous flow reactors have problems such as uneven stirring, insufficient reaction, poor material fluidity, and reaction dead zones.

[0004] Therefore, in view of this, the existing structural deficiencies are studied and improved, and a continuous flow reactor that accelerates mixing is proposed. Utility Model Content

[0005] The utility model aims to provide a continuous flow reactor for accelerating mixing, so as to solve the problems raised in the above background technology.

[0006] To achieve the above-mentioned purpose, the utility model provides the following technical solutions: a continuous flow reactor for accelerating mixing, comprising a tower reactor, wherein the tower reactor is composed of several tower sections stacked up and down, and a heat exchange jacket is arranged in the middle of the tower section, and connecting flanges are welded and fixed at the upper and lower ends of the heat exchange jacket, and the upper and lower adjacent tower sections are fixed by connecting flange bolts.

[0007] Furthermore, liquid lifting holes are provided on both sides of the bottom of the tower section, and a through hole is provided at the middle end of the bottom of the tower section.

[0008] Furthermore, conduits are fixed on both sides of the top of the tower section, and the conduits are butt-jointed with the liquid raising holes, and the joints between the conduits and the liquid raising holes are filled with sealant.

[0009] Furthermore, a butt-joint pipe is fixed to the middle end of the top of the tower section, and the butt-joint pipe is butt-jointed with the through hole, and a sealed bearing is provided at the butt joint between the butt-joint pipe and the through hole.

[0010] Furthermore, a circular array of mounting screw holes is arranged on the top of the tower section around the outer side of the butt-jointed tube, and a mixing assembly is arranged inside the tower section.

[0011] Furthermore, the mixing assembly includes a mounting plate and a driving motor, the mounting plate is fixed with bolts on the mounting screw holes, and the driving motor is fixed with bolts on the middle end of the top of the mounting plate.

[0012] Furthermore, the mixing assembly also includes a shaft, a coupling and a bearing seat. The output end of the drive motor is transmission-connected to the shaft, and both ends of the shaft are connected to the coupling. The two ends of the shaft rotate in the middle of the bearing seat, and the bearing seat is bolted to the upper and lower ends of the tower section.

[0013] Furthermore, the mixing assembly further comprises external blades and internal spiral ribbons, the external blades are arranged outside the shaft, and the internal spiral ribbons are arranged inside the shaft.

[0014] Compared with the prior art, the utility model has the following beneficial effects:

[0015] 1. When the utility model is in use, the tower reactor of the present application is composed of several tower sections stacked up and down. When in use, the upper and lower adjacent tower sections are fixed by connecting flange bolts, and the conduction of the inner cavities of the upper and lower adjacent tower sections is achieved through the cooperation of the liquid lifting hole and the conduit, and the cooperation of the through hole and the butt pipe. The tower structure design occupies a small area and improves the volume utilization rate. The number of layers and the number of uses can be designed and constructed according to actual conditions. It can be used as a single-layer reactor or a multi-layer reactor, that is, one reactor can realize the functions of multiple reactors, shorten the reaction time, reduce backmixing, and be more efficient, which can bring higher economic benefits.

[0016] 2. When the utility model is in use, during the production process, the raw material liquid enters from the feed port of the lowest tower section. When the liquid fills the current tower section, it enters the next tower section through the liquid rising hole until the liquid rises to the highest tower section and is discharged from the discharge port. The feed port located in the middle tower section can be provided with a sampling port or a plug for sealing. The present application ensures uniform heating of the solution in the tower section when using a heat exchange jacket through the provision of a mixing component. The tower section located at the highest level is fixed to the mounting plate through a reserved mounting screw hole. The driving motor is connected to the shaft through a coupling. During the rotation of the shaft, the external paddles gather the material to the center, and the internal screw belt pushes the material to the side end. Compared with the prior art that only uses paddles, the required mixing time is shorter, and the material is smoother in the reactor, thereby improving the reaction efficiency. BRIEF DESCRIPTION OF THE DRAWINGS

[0017] Figure 1 This is a schematic diagram of the overall external structure of the device of the utility model;

[0018] Figure 2 This is a schematic diagram of the overall internal structure of the device of the utility model;

[0019] Figure 3 This is a schematic diagram of the structure of the hybrid component of the utility model.

[0020] In the figure: 1. tower reactor; 2. tower section; 3. heat exchange jacket; 4. connecting flange; 5. liquid lifting hole; 6. through hole; 7. conduit; 8. butt joint; 9. mounting screw hole; 10. mixing assembly; 1001. mounting plate; 1002. drive motor; 1003. shaft; 1004. coupling; 1005. bearing seat; 1006. external blade; 1007. internal screw belt. DETAILED DESCRIPTION

[0021] The embodiments of the present utility model will be further described in detail below in conjunction with the accompanying drawings and examples. The following examples are used to illustrate the present utility model, but cannot be used to limit the scope of the present utility model.

[0022] As Figures 1 to 2 shown, a continuous flow reactor for accelerating mixing includes a tower reactor 1, which is stacked up and down by several tower sections 2. A heat exchange jacket 3 is provided in the middle of the tower section 2, and connecting flanges 4 are welded and fixed at both the upper and lower ends of the heat exchange jacket 3. Adjacent tower sections 2 are bolt-fixed through the connecting flanges 4. Liquid-lifting holes 5 are opened on both sides of the bottom of the tower section 2, and a through-hole 6 is opened in the middle of the bottom of the tower section 2. Guide pipes 7 are fixed on both sides of the top of the tower section 2, and the guide pipes 7 are in butt joint with the liquid-lifting holes 5, and sealant is filled at the butt joint of the guide pipes 7 and the liquid-lifting holes 5. A docking pipe 8 is fixed in the middle of the top of the tower section 2, and the docking pipe 8 is in butt joint with the through-hole 6, and a sealed bearing is provided at the butt joint of the docking pipe 8 and the through-hole 6. The tower reactor 1 of the present application is stacked up and down by several tower sections 2. During use, adjacent tower sections 2 are bolt-fixed through the connecting flanges 4, and the inner cavities of adjacent tower sections 2 are communicated through the cooperation of the liquid-lifting holes 5 and the guide pipes 7 and the cooperation of the through-hole 6 and the docking pipe 8. The tower structure design has a small floor area and improves the volume utilization rate. Moreover, the number of floors and the number of units can be designed and constructed according to the actual situation. It can be used as a single-layer reactor or a multi-layer reactor, that is, one reactor can realize the functions of multiple reactors, shorten the reaction time, reduce backmixing, and has higher efficiency, which can bring higher economic benefits;

[0023] As Figures 2 to 3As shown in the figure, mounting screw holes 9 are arranged in an annular array around the outer side of the docking pipe 8 at the top of the tower section 2, and a mixing assembly 10 is arranged inside the tower section 2. The mixing assembly 10 includes a mounting plate 1001 and a driving motor 1002. The mounting plate 1001 is bolted to the mounting screw holes 9, and the driving motor 1002 is bolted to the middle of the top of the mounting plate 1001. The mixing assembly 10 further includes a shaft rod 1003, a coupling 1004, and a bearing seat 1005. The output end of the driving motor 1002 is drivingly connected to the shaft rod 1003, and the two ends of the shaft rod 1003 are connected to the coupling 1004. The two ends of the shaft rod 1003 rotate in the middle of the bearing seat 1005, and the bearing seat 1005 is bolted to the upper and lower ends of the tower section 2. The mixing assembly 10 further includes an external blade 1006 and an internal spiral ribbon 1007. The external blade 1006 is arranged outside the shaft rod 1003, and the internal spiral ribbon 1007 is arranged inside the shaft rod 1003. During the production process, the raw material liquid enters from the feed port of the lowermost tower section 2. When the liquid fills the current tower section 2, it enters the next tower section 2 through the lifting hole 5 until the liquid rises to the topmost tower section 2 and is discharged from the discharge port. A sampling port can be arranged at the feed port of the middle tower section 2 or plugged with a plug. Through the arrangement of the mixing assembly 10 in this application, the solution in the tower section 2 is ensured to be evenly heated when using the heat exchange jacket 3. The topmost tower section 2 fixes the mounting plate 1001 through the reserved mounting screw holes 9. The driving motor 1002 is drivingly connected to the shaft rod 1003 through the coupling 1004. During the rotation of the shaft rod 1003, the external blade 1006 gathers the materials to the center, and then the internal spiral ribbon 1007 pushes the materials to the side end. Compared with the prior art that only uses blades, the required mixing time is shorter, and the materials are flatter in the reactor, improving the reaction efficiency.

[0024] Working principle: When using this kind of continuous flow reactor that accelerates mixing, the tower reactor 1 of the present application is composed of several tower sections 2 stacked up and down. When in use, the upper and lower adjacent tower sections 2 are fixed by connecting flanges 4 bolts, and the cooperation of the liquid lifting hole 5 and the conduit 7 and the cooperation of the through hole 6 and the docking pipe 8 realizes the conduction of the inner cavity of the upper and lower adjacent tower sections 2. The tower structure design occupies a small area and improves the volume utilization rate. The number of layers and the number of uses can be designed and constructed according to actual conditions. It can be used as a single-layer reactor or a multi-layer reactor, that is, one reactor can realize the functions of multiple reactors, shorten the reaction time, reduce back mixing, and be more efficient, which can bring higher economic benefits. During the production process, the raw liquid enters from the feed port of the lowest tower section 2. When the liquid is filled The liquid in the current tower section 2 enters the next tower section 2 through the liquid rising hole 5 until the liquid rises to the highest tower section 2 and is discharged from the discharge port. The feed port of the middle tower section 2 can be provided with a sampling port or a plug for sealing. The present application ensures that the solution in the tower section 2 is heated evenly when the heat exchange jacket 3 is used by providing a mixing component 10. The tower section 2 located at the highest level is fixed to the mounting plate 1001 through the reserved mounting screw hole 9. The driving motor 1002 is connected to the shaft 1003 through the coupling 1004. During the rotation of the shaft 1003, the external paddles 1006 gather the material to the center, and then the internal screw belt 1007 pushes the material to the side end. Compared with the prior art that only uses paddles, the required mixing time is shorter, and the material is smoother in the reactor, thereby improving the reaction efficiency.

[0025] The embodiments of the present invention are provided for the purpose of illustration and description, and are not intended to be exhaustive or to limit the present invention to the disclosed forms. Many modifications and variations will be apparent to those of ordinary skill in the art. The embodiments are selected and described to better illustrate the principles and practical applications of the present invention, and to enable those of ordinary skill in the art to understand the present invention and thereby design various embodiments with various modifications suitable for specific uses.

Claims

1. A continuous flow reactor for accelerating mixing, comprising a tower reactor (1), characterized in that, The tower reactor (1) is formed by stacking several tower sections (2) up and down. A heat exchange jacket (3) is provided in the middle of the tower section (2), and connecting flanges (4) are welded and fixed at the upper and lower ends of the heat exchange jacket (3). The adjacent upper and lower tower sections (2) are bolted together through the connecting flanges (4).

2. The continuous flow reactor for accelerating mixing according to claim 1, wherein Liquid-lifting holes (5) are formed on both sides of the bottom of the tower section (2), and a through hole (6) is formed in the middle of the bottom of the tower section (2).

3. A continuous flow reactor for accelerating mixing according to claim 1, characterized in that, Conduits (7) are fixed on both sides of the top of the tower section (2), and the conduits (7) are in butt joint with the liquid-lifting holes (5). Sealant is filled at the butt joint of the conduits (7) and the liquid-lifting holes (5).

4. A continuous flow reactor for accelerating mixing according to claim 1, characterized in that A butt joint pipe (8) is fixed in the middle of the top of the tower section (2), and the butt joint pipe (8) is in butt joint with the through hole (6). A sealed bearing is provided at the butt joint of the butt joint pipe (8) and the through hole (6).

5. A continuous flow reactor for accelerating mixing according to claim 1, characterized in that, Mounting screw holes (9) are arranged in an annular array around the outer side of the butt joint pipe (8) at the top of the tower section (2), and a mixing assembly (10) is arranged inside the tower section (2).

6. A continuous flow reactor for accelerating mixing according to claim 5, characterized in that, The mixing assembly (10) includes a mounting plate (1001) and a driving motor (1002). The mounting plate (1001) is bolted to the mounting screw holes (9), and the driving motor (1002) is bolted to the middle of the top of the mounting plate (1001).

7. The continuous flow reactor for accelerating mixing according to claim 6, wherein, The mixing assembly (10) further includes a shaft rod (1003), a coupling (1004), and a bearing seat (1005). The output end of the driving motor (1002) is drivingly connected to the shaft rod (1003), and the two ends of the shaft rod (1003) are connected with the coupling (1004). The two ends of the shaft rod (1003) rotate in the middle of the bearing seat (1005), and the bearing seat (1005) is bolted to the upper and lower ends of the tower section (2).

8. A continuous flow reactor for accelerating mixing according to claim 7, characterized in that, The mixing assembly (10) further includes an external paddle (1006) and an internal spiral ribbon (1007). The external paddle (1006) is arranged outside the shaft rod (1003), and the internal spiral ribbon (1007) is arranged inside the shaft rod (1003).

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