A liquefaction reaction conveying device

Abstract

A liquefaction reaction conveying device has a tank inlet at the top and a tank outlet at the bottom. The tank is equipped with a heating device that is spirally distributed and forms a spiral enclosed space. A gasification pipeline is installed inside the spiral enclosed space and is connected to the tank inlet and the tank outlet, which effectively improves the heating efficiency and gasification efficiency of the conveying device.

Description

Technical Field

[0001] This application relates to the technical field of gas transportation, and in particular to a liquefaction reaction transportation device. Background Technology

[0002] Liquefied gases are substances that can be converted from gas to liquid under certain pressure through compression, cooling, or other methods. Because liquid gases have a wide variety of types and properties, they are widely used in many fields, such as household, industrial, and medical fields.

[0003] In the prior art, chloroethane is widely used in industry, usually as a fuel and chemical raw material. During the pipeline transportation process, liquefied chloroethane is usually transported to the designated location in the form of gas, and the liquid chloroethane in the transportation device is usually heated to convert it into a gaseous state. However, in the existing technology, the heating efficiency of the heating tube in the conveying device is low, and the gasification efficiency of the liquefied gas is poor. Utility Model Content

[0004] This utility model provides a liquefaction reaction conveying device that effectively improves the heating efficiency and gasification efficiency of the conveying device.

[0005] To achieve the aforementioned objectives, this application adopts the following technical solution: A liquefaction reaction conveying device, comprising The tank has an inlet at the top and an outlet at the bottom. A heating device is installed inside the tank, which is spirally distributed and forms a spiral enclosed space. A vaporization pipe is installed inside the spiral enclosed space, which is spirally shaped and connected to the inlet and outlet of the tank.

[0006] In some alternative implementations, the gasification pipeline includes an A end and a B end.

[0007] In some alternative embodiments, end A of the gasification pipeline is connected to the tank inlet, and end B is connected to the tank outlet.

[0008] In some alternative embodiments, the sidewalls of the vaporization pipeline are corrugated.

[0009] In some alternative embodiments, the outer wall of the vaporization conduit is coated with a graphene coating.

[0010] In some alternative embodiments, the outer wall of the vaporization conduit faces the heating device.

[0011] In some alternative embodiments, the bottom of the tank is also provided with a support device.

[0012] In some alternative embodiments, the heating device is located in the lower middle part of the tank body to form a space that is divided into a liquid flow space and a gas-liquid coexistence space during the liquefied gas transportation process.

[0013] The liquefaction reaction conveying device provided in this application has the following beneficial effects: In the technical solution adopted in this application, a liquefaction reaction conveying device is provided. A heating device is set in the middle and lower part of the tank, and a gasification pipeline is set in the spiral space surrounded by the heating device. The heating device heats the gasification pipeline. The gasification pipeline is spiral in shape. The A end of the gasification pipeline is connected to the tank inlet, and the B end is connected to the tank outlet. The side wall of the gasification pipeline is corrugated, and a graphene layer is coated on the outer side wall of the gasification pipeline, which effectively improves the heating efficiency and gasification efficiency in the conveying device. Attached Figure Description

[0014] Other features, objects, and advantages of this application will become more apparent from the following detailed description of non-limiting embodiments with reference to the accompanying drawings: Figure 1 This is a schematic diagram of the structure of a liquefaction reaction conveying device according to this application; Figure 2 This is a schematic diagram of the internal structure of a liquefaction reaction conveying device according to this application; Figure 3 This is a partial structural diagram of the gasification pipeline in a liquefaction reaction conveying device according to this application; Figure 4 This is a layered structure diagram of the sidewall of the gasification pipeline in a liquefaction reaction conveying device according to this application.

[0015] Figure label: 10. Tank body; 11. Tank inlet; 12. Tank outlet; 13. Supporting device; 20. Heating device; 21. Spiral enclosing space; 22. Gasification pipeline; 23. Corrugated sidewall; 24. Graphene coating. Detailed Implementation

[0016] The specific embodiments of this application are described below with reference to the accompanying drawings and examples. Through the content described in this specification, those skilled in the art can clearly and completely understand the technical solution, the technical problem solved, and the resulting technical effects of this application. It is understood that the specific embodiments described herein are only for explaining this application and not for limiting it. Furthermore, for ease of description, only the parts related to this application are shown in the accompanying drawings.

[0017] It should be noted that the structures, proportions, sizes, etc., shown in the accompanying drawings are only for the purpose of assisting those skilled in the art in understanding and reading the contents described in the specification, and are not intended to limit the conditions under which this application can be implemented. Therefore, they have no substantial technical significance. Any modifications to the structure, changes in the proportional relationships, or adjustments to the size should fall within the scope of the technical content disclosed in this application, provided that they do not affect the effects and purposes that this application can produce.

[0018] The use of terms such as "first," "second," and "the" does not imply quantity limitation and may indicate singular or plural. The terms "comprising," "including," "having," and any variations thereof used in this application are intended to cover non-exclusive inclusion; for example, processes, methods, systems that include a series of steps or modules. The product or equipment is not limited to the listed steps or units, but may also include steps or units not listed, or other steps or units inherent to these processes, methods, products, or equipment. Terms such as “connection,” “linking,” and “coupled” used in this application are not limited to physical or mechanical connections, but may also include direct or indirect electrical connections.

[0019] It should also be noted that the longitudinal section corresponding to the embodiment of this application can be the section corresponding to the front view direction, the transverse section can be the section corresponding to the right view direction, and the horizontal section can be the section corresponding to the top view direction.

[0020] Furthermore, where there is no conflict, the embodiments and features described in this application can be combined with each other. This application will now be described in detail with reference to the accompanying drawings and embodiments.

[0021] refer to Figure 1 , Figure 1 This is a schematic diagram of the structure of a liquefaction reaction conveying device according to this application. Figure 1 As shown, a liquefaction reaction conveying device includes a tank 10, with a tank inlet 11 at the top and a tank outlet 12 at the bottom, and a support device 13 at the bottom of the tank 10.

[0022] Continue to refer to Figure 1 Please refer to them together. Figure 2 and Figure 3 , Figure 2 This is a schematic diagram of the internal structure of a liquefaction reaction conveying device according to this application. Figure 3 This is a partial structural diagram of the gasification pipeline in a liquefaction reaction conveying device according to this application. Figure 1 , Figure 2 and Figure 3As shown, a heating device 20 is installed inside the tank 10. The heating device 20 is located in the lower middle part of the tank 10, forming a space for liquid flow and a space for gas-liquid coexistence during the liquefied gas transportation process. The heating device 20 is spirally distributed to expand the heating area and improve heating efficiency. A spiral-enclosed space 21 is formed inside the heating device 20. A vaporization pipe 22 is installed inside the spiral-enclosed space 21. The outer wall of the vaporization pipe 22 faces the heating device 20. The vaporization pipe 22 is spirally shaped and connects to the tank inlet 11 and the tank outlet 12. This increases the transportation distance of the pipe within the limited space of the tank 10, thereby improving the heating and vaporization efficiency of the liquefied gas in the transportation device. Specifically, the vaporization pipe 22 includes an A end and a B end. The A end of the vaporization pipe 22 is connected to the tank inlet 11, and its B end is connected to the tank outlet 12.

[0023] Continue to refer to Figure 3 Please refer to them together. Figure 4 , Figure 4 This is a layered structural diagram of the sidewall of the gasification pipeline in a liquefaction reaction conveying device according to this application. (See diagram for reference.) Figure 3 and Figure 4 As shown, the sidewall of the vaporization pipeline 22 is further corrugated 23. The corrugated sidewall 23 increases the heating area during the transport of liquefied gas and during the heating of the vaporization pipeline 22 by the heating device 20, thereby improving heating efficiency and vaporization efficiency. Furthermore, the outer sidewall of the vaporization pipeline 22 is covered with a graphene coating 24. By coating the outer sidewall of the vaporization pipeline 22 with a graphene coating 24, the heat conversion rate is effectively improved during the heating of the vaporization pipeline 22 by the heating device 20, thereby improving heating efficiency and further optimizing vaporization efficiency. Here, a liquefaction reaction conveying device is provided. A heating device 20 is installed in the lower middle part of the tank 10. A gasification pipeline 22 is installed in the spiral space 21 surrounded by the heating device 20. The heating device 20 heats the gasification pipeline 22, which is spiral in shape. The A end of the gasification pipeline 22 is connected to the tank inlet 11, and the B end is connected to the tank outlet 12. The side wall of the gasification pipeline 22 is a corrugated side wall 23, and a graphene layer is coated on the outer side wall of the gasification pipeline 22. This effectively improves the heating efficiency and gasification efficiency of the conveying device.

[0024] Although this application has been described and illustrated with reference to specific embodiments thereof, such description and illustration are not limiting of this application. It will be readily understood by those skilled in the art that various changes can be made and equivalent elements can be substituted within embodiments without departing from the true spirit and scope of this application as defined by the appended claims. Illustrations may not be drawn to scale. Differences may exist between the technical representation in this application and actual implementation due to variables in the manufacturing process, etc. Other embodiments of this application may exist that are not specifically described. The description and illustrations should be considered illustrative rather than restrictive. Modifications can be made to adapt particular circumstances, materials, composition, methods, or processes to the objectives, spirit, and scope of this application. All such modifications fall within the scope of the appended claims. While the methods disclosed herein have been described with reference to specific operations performed in a particular order, it should be understood that these operations can be combined, subdivided, or reordered to form equivalent methods without departing from the teachings of this application. Therefore, unless specifically indicated herein, the order and grouping of operations do not limit this application.

Claims

1. A liquefaction reaction conveying device, characterized in that, include The tank (10) has a tank inlet (11) at the top and a tank outlet (12) at the bottom. The tank (10) is equipped with a heating device (20) inside. The heating device (20) is spirally distributed and forms a spiral enclosed space (21) inside. The spiral enclosed space (21) is equipped with a gasification pipe (22) inside. The gasification pipe (22) is spirally connected to the tank inlet (11) and the tank outlet (12).

2. The liquefaction reaction conveying device according to claim 1, characterized in that, The gasification pipeline (22) includes end A and end B.

3. The liquefaction reaction conveying device according to claim 2, characterized in that, The A end of the gasification pipeline (22) is connected to the tank inlet (11), and the B end is connected to the tank outlet (12).

4. The liquefaction reaction conveying device according to claim 3, characterized in that, The sidewall of the gasification pipeline (22) is a corrugated sidewall (23).

5. The liquefaction reaction conveying device according to claim 4, characterized in that, The outer wall of the gasification pipeline (22) is covered with a graphene coating (24).

6. The liquefaction reaction conveying device according to claim 5, characterized in that, The outer wall of the gasification pipe (22) faces the heating device (20).

7. The liquefaction reaction conveying device according to claim 6, characterized in that, The bottom of the tank (10) is also provided with a support device (13).

8. The liquefaction reaction conveying device according to claim 7, characterized in that, The heating device (20) is located in the lower middle part inside the tank (10) to form a liquid flow space and a gas-liquid coexistence space during the liquefied gas transportation process.

Images