Novel continuous reactor device

Abstract

The utility model discloses a novel continuous reactor device which comprises a tubular reactor, a first feed pipe is communicated and connected with the top of the tubular reactor close to the left side, and second feed pipes are respectively communicated and connected with the bottom of the tubular reactor close to the left side and the right side. The top end of the first feeding pipe and the bottom ends of the two second feeding pipes are respectively communicated and connected with an SK mixer, a combined SK mixer is arranged in the tubular reactor, and a heat exchange medium inlet is communicated and connected to the left side, close to the bottom, of the tubular reactor. According to the technical scheme, through mutual cooperation of the tubular reactor, the SK mixer, the combined SK mixer and other components, adding and continuous production of various materials at different time can be achieved, the SK mixer set is connected in parallel in the tubular reactor, the solution mixing and reaction efficiency is higher, the heat exchange efficiency is higher, local temperature rise is avoided, and the production efficiency is improved. And the reaction heat can be effectively utilized to supply heat to the two-stage reaction.

Description

Technical Field

[0001] This utility model relates to the field of reactor technology, and in particular to a novel continuous reactor device. Background Technology

[0002] A reactor is an engineering device used to realize chemical, physical, or biological reactions. Its core function is to provide suitable conditions (such as temperature, pressure, and mixing state) to promote material transformation or energy exchange. However, existing reactor devices cannot achieve the addition of multiple materials at different times or continuous production, resulting in reduced solution mixing and reaction efficiency, lower heat exchange efficiency, and the inability to avoid localized heating. Consequently, they cannot effectively utilize the heat of reaction to supply heat to the two stages of the reaction. Therefore, we propose a novel continuous reactor device. Utility Model Content

[0003] The purpose of this invention is to at least solve one of the technical problems existing in the prior art, and to provide a new type of continuous reactor device that is suitable for continuous reaction, can realize the addition of various materials at different times and continuous production. The tube reactor is connected in parallel with an SK mixer group, which makes the solution mixing and reaction efficiency higher, the heat exchange efficiency higher, avoids local heating, and can effectively utilize the heat of reaction to supply heat to the two-stage reaction.

[0004] To achieve the above objectives, a novel continuous reactor device is provided, comprising: a tubular reactor, wherein a first feed pipe is connected to the top of the tubular reactor near the left side, and second feed pipes are respectively connected to the bottom of the tubular reactor near the left and right sides, and an SK mixer is respectively connected to the top of the first feed pipe and the bottom of the two second feed pipes.

[0005] According to the novel continuous reactor device, a combined SK mixer is installed inside the tubular reactor, and a heat exchange medium inlet is connected to the left side of the tubular reactor near the bottom.

[0006] According to the novel continuous reactor device, a heat exchange medium outlet is connected to the right side of the tubular reactor near the top, and an outlet E is connected to the top of the tubular reactor near the right side.

[0007] According to the novel continuous reactor device, the combined SK mixer is located near the top inside the tube reactor, and the heat exchange medium outlet is located on the right side of the combined SK mixer near the bottom.

[0008] According to the novel continuous reactor device, the upper SK mixer is located above the tubular reactor near the left side, and the lower SK mixer is located below the tubular reactor near the right side.

[0009] The above solution has at least one of the following beneficial effects: This technical solution, through the cooperation between components such as the tubular reactor, SK mixer and combined SK mixer, enables the addition of multiple materials at different times and continuous production. The SK mixer group is connected in parallel inside the tubular reactor, which makes the solution mixing and reaction efficiency higher, the heat exchange efficiency higher, avoids local heating, and can effectively utilize the heat of reaction to supply heat to the two-stage reaction.

[0010] Additional aspects and advantages of this invention will be set forth in part in the description which follows, and in part will be obvious from the description, or may be learned by practice of the invention. Attached Figure Description

[0011] The present invention will be further described below with reference to the accompanying drawings and embodiments;

[0012] Figure 1 This is a schematic diagram of the main structure of this utility model;

[0013] Figure 2 for Figure 1 A partial structural diagram of the combined SK mixer and its components.

[0014] Figure 3 for Figure 1 Enlarged view of point F in the image.

[0015] Legend:

[0016] 1. Tubular reactor; 2. SK mixer; 3. Combined SK mixer; 4. Heat exchange medium inlet; 5. Heat exchange medium outlet; 6. Outlet E. Detailed Implementation

[0017] This section will describe in detail the specific embodiments of the present utility model. The preferred embodiments of the present utility model are shown in the accompanying drawings. The purpose of the drawings is to supplement the textual description with graphics, so that people can intuitively and vividly understand each technical feature and the overall technical solution of the present utility model, but they should not be construed as limiting the scope of protection of the present utility model.

[0018] Reference Figures 1 to 3This utility model provides a novel continuous reactor device, which includes a tubular reactor 1. The top of the tubular reactor 1 is connected to a first feed pipe 7 near the left side, and the bottom of the tubular reactor 1 is connected to second feed pipes 8 near the left and right sides respectively. The top of the first feed pipe 7 and the bottom of the two second feed pipes 8 are respectively connected to an SK mixer 2.

[0019] A combined SK mixer 3 is installed inside the tubular reactor 1. A heat exchange medium inlet 4 is connected to the bottom left side of the reactor 1, and a heat exchange medium outlet 5 is connected to the top right side. An outlet E6 is connected to the top right side of the reactor 1. The combined SK mixer 3 is located near the top of the reactor 1, with the heat exchange medium outlet 5 located near the bottom right side of the combined SK mixer 3. An upper SK mixer 2 is located above the reactor 1 near the left side, and a lower SK mixer 2 is located below the reactor 1 near the right side. This structure allows for the addition of multiple materials at different times and continuous production. The parallel connection of the SK mixer group inside the tubular reactor results in higher solution mixing and reaction efficiency, higher heat exchange efficiency, avoidance of localized temperature rise, and effective utilization of reaction heat to supply heat to both stages of the reaction.

[0020] Working principle: When using this technical solution, firstly, a fixed amount of liquid raw material ABC is efficiently mixed through SK mixer 2. After mixing, the material enters the tubular reactor 1. After passing through the internal combined SK mixer 3, it undergoes multiple mixing reactions. After the reaction, the liquid exits the system. Then it is mixed with raw material D and enters the tubular reactor 1 again for another mixing reaction. Finally, the qualified product is discharged from the outlet E6.

[0021] The foregoing has shown and described the basic principles, main features, and advantages of this utility model. Those skilled in the art should understand that this utility model is not limited to the above embodiments. The embodiments and descriptions in the specification are merely illustrative of the principles of this utility model. Various changes and modifications can be made to this utility model without departing from its spirit and scope, and all such changes and modifications fall within the scope of the claims. The scope of protection of this utility model is defined by the appended claims and their equivalents.

Claims

1. A novel continuous reactor device, characterized in that, include: The tubular reactor (1) has a first feed pipe (7) connected to the top near the left side, and a second feed pipe (8) connected to the bottom near the left and right sides respectively. The top of the first feed pipe (7) and the bottom of the two second feed pipes (8) are respectively connected to an SK mixer (2).

2. The novel continuous reactor device according to claim 1, characterized in that, The tubular reactor (1) is equipped with a combined SK mixer (3), and a heat exchange medium inlet (4) is connected to the left side of the tubular reactor (1) near the bottom.

3. The novel continuous reactor device according to claim 2, characterized in that, The right side of the tubular reactor (1) is connected to a heat exchange medium outlet (5) near the top, and the top of the tubular reactor (1) is connected to an outlet E (6) near the right side.

4. The novel continuous reactor device according to claim 3, characterized in that, The combined SK mixer (3) is located near the top inside the tube reactor (1), and the heat exchange medium outlet (5) is located on the right side of the combined SK mixer (3) near the bottom.

5. A novel continuous reactor device according to claim 1, characterized in that, The upper SK mixer (2) is located above the tubular reactor (1) near the left side, and the lower SK mixer (2) is located below the tubular reactor (1) near the right side.

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