Horizontal nested container
Through the horizontal nested container design, the inner cylinder pressure is transferred to the outer cylinder by using a transfer member, which solves the problem of reduced heat exchange capacity under high pressure, achieves efficient heat exchange and structural stability, and improves the safety and heat exchange efficiency of the container.
Patent Information
- Application Number
- CN202422640308.4
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-10-30
- Publication Date
- 2025-10-10
- Estimated Expiration
- 2034-10-30
AI Technical Summary
Under high pressure or large diameter conditions, the wall thickness of the inner tube of the existing jacketed reaction vessel increases, which increases thermal resistance and reduces heat exchange capacity.
A horizontal sleeve container design is adopted, and the pressure load of the inner cylinder is transferred to the outer cylinder through the transmission parts. The outer cylinder bears most of the pressure load through the sleeve structure and realizes efficient heat exchange through the thinner wall thickness of the inner cylinder.
The structural strength and stability of the container are enhanced to ensure safety, while the heat exchange efficiency is improved, the thermal resistance is reduced, and efficient heat transfer and heat exchange are achieved.
Smart Images
Figure CN223417266U_ABST
Abstract
Description
Technical Field
[0001] The present application relates to the technical field of production equipment, and in particular to a horizontal sleeve container. Background Art
[0002] Jacketed containers are important equipment in the production process of various chemicals. They provide suitable pressure and temperature environments for the reaction process of process media. They should ensure that the container can withstand internal pressure safely and reliably while providing sufficient heat exchange capacity.
[0003] Currently, commonly used jacketed reaction vessels include full jacketed vessels, half-tube jacketed vessels, honeycomb jacketed vessels, etc. When the reaction pressure in the reaction vessel is high or the vessel diameter is large, the inner tube wall thickness increases, increasing thermal resistance and reducing heat exchange capacity.
[0004] The preceding description is intended to provide general background information and does not necessarily constitute prior art.
[0005] Application Contents
[0006] The main purpose of this application is to provide a horizontal sleeve container that can withstand high pressure in the inner cylinder while meeting the requirements of efficient heat exchange.
[0007] To achieve the above objectives, in a first aspect, the present application provides a horizontal nested container, comprising:
[0008] The cylinder assembly includes an outer cylinder and an inner cylinder. The outer cylinder is sleeved on the outer circumference of the inner cylinder. The inner cylinder has a receiving cavity for receiving materials.
[0009] The cylinder assembly also has a heat exchange channel, which is formed between the outer cylinder and the inner cylinder. The heat exchange channel is used to inject heat exchange medium, and the heat exchange medium flows in the heat exchange channel to exchange heat with the material in the accommodating cavity;
[0010] The transfer member is arranged in the heat exchange channel and is located between the outer cylinder and the inner cylinder to transfer the pressure of the inner cylinder to the outer cylinder.
[0011] The beneficial effects of this application are as follows: through the provision of transfer members, the pressure load of the process medium is transmitted to the outer cylinder through the raised transfer members on both sides of the heat exchange channel on the inner cylinder. The transfer members not only enhance the structural strength of the inner cylinder but also effectively disperse the pressure to the outer cylinder. The outer cylinder, through the nested structure, bears the majority of the reaction pressure load, ensuring the safety and stability of the container under high-pressure conditions. Under high pressure conditions within the container, the thinner inner cylinder wall design enables efficient heat transfer and heat exchange. The thin-wall design reduces thermal resistance and improves heat exchange efficiency.
[0012] Based on the above technical solution, this application can also be improved as follows.
[0013] In some optional embodiments, a material inlet and a material outlet are provided on the barrel assembly, and both the material inlet and the material outlet are communicated with the accommodating chamber.
[0014] It should be noted that the setting of the material inlet and material outlet satisfies the addition and export of materials.
[0015] In some optional embodiments, a heat exchange medium inlet and a heat exchange medium outlet are provided on the cylinder assembly, and both the heat exchange medium inlet and the heat exchange medium outlet are connected to the heat exchange channel.
[0016] It should be noted that the arrangement of the heat exchange medium inlet and outlet allows the heat exchange medium to efficiently enter and exit the heat exchange channel, ensuring an optimized flow path within the channel, thereby improving heat exchange efficiency. By properly arranging the heat exchange medium inlet and outlet, the heat exchange medium can be evenly distributed within the heat exchange channel, avoiding localized overheating or overcooling and ensuring uniform heating or cooling of the material throughout the container.
[0017] In some optional embodiments, there are multiple transmission members, and the multiple transmission members are spaced apart and located between the outer cylinder and the inner cylinder.
[0018] It should be noted that multiple transmission members are arranged at intervals between the outer cylinder and the inner cylinder, which can evenly distribute the pressure load of the process medium, reduce local stress concentration, and enhance the overall structural strength and stability of the container.
[0019] In some optional embodiments, one end of the transmission member is disposed on the inner wall of the outer cylinder, and the other end of the transmission member extends toward the inner cylinder with a first gap between the transmission member and the inner cylinder.
[0020] It should be noted that one end of the transmission member is fixed on the inner wall of the outer cylinder, and the other end extends toward the inner cylinder with a first gap, which can evenly distribute the pressure load of the process medium, reduce local stress concentration, and enhance the overall structural strength and stability of the container.
[0021] In some optional embodiments, one end of the transmission member is disposed on the outer wall of the inner cylinder, and the other end of the transmission member extends toward the outer cylinder with a second gap between the transmission member and the outer cylinder.
[0022] It should be noted that multiple transfer parts are designed between the outer cylinder and the inner cylinder, and one end of the transfer part is fixed on the outer wall of the inner cylinder, and the other end extends toward the outer cylinder with a second gap between the outer cylinder and the outer cylinder. This can significantly enhance the structural strength and stability of the container, optimize the heat exchange effect, evenly distribute thermal stress, simplify the manufacturing and maintenance process, improve safety and reliability, and flexibly adapt to different process requirements.
[0023] In some optional embodiments, the barrel assembly is provided with a stirring port, which is communicated with the accommodating cavity;
[0024] At least two stirring ports are located on opposite sides of the barrel assembly along the second direction.
[0025] It should be noted that multiple stirring ports facilitate multi-point stirring to improve the uniformity of material mixing.
[0026] In some optional embodiments, the material inlet and the material outlet are located on opposite sides of the accommodating cavity along the first direction.
[0027] It should be noted that the material inlet and outlet are located on opposite sides of the receiving chamber along the first direction, which allows the material to flow in a straight line within the receiving chamber, reducing flow resistance and retention, and improving material flow efficiency. This helps to evenly distribute the material within the receiving chamber, avoids local accumulation, and ensures uniformity and stability of the process.
[0028] In some optional embodiments, the horizontal nested container further includes an agitator, and the agitator rotates within the accommodating cavity.
[0029] It should be noted that the introduction of the agitator can effectively mix the materials in the containing chamber, ensure the uniform distribution of the materials, avoid local concentration differences, and improve the uniformity and stability of the process.
[0030] In some optional embodiments, the transmission member is a fin; and / or,
[0031] The transmission member is an integrally formed structure with one of the outer cylinder and the inner cylinder.
[0032] It should be noted that by designing the transfer member as a fin, and the transfer member and one of the outer cylinder and the inner cylinder as an integrally molded structure, the structural strength and stability of the container can be significantly enhanced, the heat exchange efficiency and uniformity can be improved, the manufacturing and maintenance process can be simplified, the safety and reliability can be improved, and it can be flexibly adapted to different process requirements.
[0033] The horizontal nested container provided in the present application includes: a cylinder assembly, the cylinder assembly includes an outer cylinder and an inner cylinder, the outer cylinder is sleeved on the outer periphery of the inner cylinder, the inner cylinder has a accommodating cavity, and the accommodating cavity is used to accommodate materials; the cylinder assembly also has a heat exchange channel, a heat exchange channel is formed between the outer cylinder and the inner cylinder, the heat exchange channel is used to inject heat exchange medium, the heat exchange medium flows in the heat exchange channel to exchange heat with the material in the accommodating cavity; a transfer member, the transfer member is arranged in the heat exchange channel and is located between the outer cylinder and the inner cylinder to transfer the pressure of the inner cylinder to the outer cylinder.
[0034] The transfer elements transmit the pressure load of the process medium to the outer cylinder via the raised transfer elements on either side of the heat exchange channel on the inner cylinder. These transfer elements not only enhance the structural strength of the inner cylinder but also effectively distribute the pressure to the outer cylinder. The outer cylinder, through its sleeved structure, bears the majority of the reaction pressure load, ensuring the safety and stability of the vessel under high-pressure conditions. Even under high pressures, the thinner inner cylinder wall allows for efficient heat transfer and exchange. This thin-wall design reduces thermal resistance and improves heat exchange efficiency. BRIEF DESCRIPTION OF THE DRAWINGS
[0035] In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, a brief introduction will be given below to the drawings required for use in the embodiments or the description of the prior art. Obviously, the drawings described below are some embodiments of the present application. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying any creative labor.
[0036] Figure 1 A schematic structural diagram of a horizontal nested container provided in an embodiment of the present application;
[0037] Figure 2 A side sectional view of a horizontal nested container provided in an embodiment of the present application;
[0038] Figure 3 A schematic structural diagram of another horizontal nested container provided in an embodiment of the present application;
[0039] Figure 4 A side sectional view of another horizontal nested container provided in an embodiment of the present application.
[0040] Description of reference numerals:
[0041] 100-Horizontal sleeve container;
[0042] 110-cylinder assembly;
[0043] 111-Outer cylinder;
[0044] 112-Inner cylinder;
[0045] 113-Material entrance;
[0046] 114-Material export;
[0047] 115-heat exchange medium inlet;
[0048] 116-heat exchange medium outlet;
[0049] 117- stirring port;
[0050] 118-heat exchange channel;
[0051] 119-manhole;
[0052] 120-transmission parts;
[0053] 130-Agitator. DETAILED DESCRIPTION
[0054] In order to make the purpose, technical solutions and advantages of the embodiments of the present application clearer, the technical solutions in the embodiments of the present application will be clearly and completely described below in conjunction with the drawings in the embodiments of the present application. Obviously, the described embodiments are part of the embodiments of the present application, not all of the embodiments. Based on the embodiments in this application, all other embodiments obtained by ordinary technicians in this field without making creative work are within the scope of protection of this application. All other embodiments obtained are within the scope of protection of this application. In the absence of conflict, the following embodiments and features in the embodiments can be combined with each other.
[0055] In this application, unless otherwise specified or limited, the terms "installed," "connected," "connect," "fixed," etc. should be understood in a broad sense. For example, they can refer to fixed connection, detachable connection, or integration; mechanical connection or electrical connection; direct connection or indirect connection through an intermediate medium; internal communication between two elements or interaction between two elements, unless otherwise specified. Those skilled in the art will understand the specific meanings of the above terms in this application based on specific circumstances.
[0056] In this application, unless otherwise expressly specified or limited, when a first feature is "above" or "below" a second feature, it may mean that the first and second features are in direct contact, or the first and second features are in indirect contact through an intermediate medium. Furthermore, when a first feature is "above," "above," or "above" a second feature, it may mean that the first feature is directly above or diagonally above the second feature, or simply means that the first feature is at a higher level than the second feature. When a first feature is "below," "below," or "below" a second feature, it may mean that the first feature is directly below or diagonally below the second feature, or simply means that the first feature is at a lower level than the second feature.
[0057] In the description of this specification, the description with reference to the terms "one embodiment", "some embodiments", "example", "specific example", or "some examples" means that the specific features, structures, materials or characteristics described in conjunction with the embodiment or example are included in at least one embodiment or example of the present application. In this specification, the schematic representations of the above terms do not necessarily refer to the same embodiment or example. Moreover, the specific features, structures, materials or characteristics described can be combined in any one or more embodiments or examples in a suitable manner. In addition, those skilled in the art can combine and combine different embodiments or examples described in this specification and features of different embodiments or examples without contradiction.
[0058] At present, the commonly used jacketed reaction vessels include full jacketed vessels, half-tube jacketed vessels, honeycomb jacketed vessels, etc. When the reaction pressure in the reaction vessel is high or the vessel diameter is large, the inner tube wall thickness becomes larger, which increases the thermal resistance and reduces the heat exchange capacity.
[0059] In order to overcome the defects in the prior art, the horizontal sleeve container provided by the present application transmits the pressure load of the process medium to the outer cylinder through the raised transfer members on both sides of the heat exchange channel on the inner cylinder through the setting of the transfer member. The transfer member not only enhances the structural strength of the inner cylinder, but also effectively disperses the pressure to the outer cylinder, that is, it can meet the requirements of efficient heat exchange while the inner cylinder is subjected to higher pressure; the outer cylinder bears most of the pressure load of the reaction through the sleeve structure, ensuring the safety and stability of the container under high pressure conditions; when the pressure inside the container is high, by designing a thinner inner cylinder wall thickness, efficient heat transfer and heat exchange effects can be achieved. The thin-wall design reduces thermal resistance and improves heat exchange efficiency.
[0060] The contents of this application will be described in detail below with reference to the accompanying drawings so that those skilled in the art can understand the contents of this application more clearly and in detail.
[0061] Figure 1 This is a schematic diagram of the structure of a horizontal nested container provided in an embodiment of the present application. Figure 2 This is a side sectional view of a horizontal nested container provided in an embodiment of the present application. Figure 3 This is a schematic diagram of the structure of another horizontal nested container provided in an embodiment of the present application. Figure 4 A side sectional view of another horizontal nested container provided in an embodiment of the present application.
[0062] like Figures 1 to 4 As shown, the embodiment of the present application provides a horizontal nested container 100, comprising:
[0063] The barrel assembly 110 includes an outer barrel 111 and an inner barrel 112. The outer barrel 111 is sleeved on the outer circumference of the inner barrel 112. The inner barrel 112 has a receiving cavity for receiving materials.
[0064] The barrel assembly 110 further has a heat exchange channel 118 formed between the outer barrel 111 and the inner barrel 112. The heat exchange channel 118 is used to inject a heat exchange medium. The heat exchange medium flows in the heat exchange channel 118 to exchange heat with the material in the accommodating cavity.
[0065] The transmission member 120 is disposed in the heat exchange channel 118 and located between the outer cylinder 111 and the inner cylinder 112 to transmit the pressure of the inner cylinder 112 to the outer cylinder 111 .
[0066] Through the above-described arrangement, namely, the provision of transfer members 120, the pressure load of the process medium is transmitted to the outer cylinder 111 via the raised transfer members 120 on both sides of the heat exchange channel 118 on the inner cylinder 112. Transfer members 120 not only enhance the structural strength of the inner cylinder 112 but also effectively disperse the pressure onto the outer cylinder 111. The outer cylinder 111, through its nested structure, bears the majority of the reaction's pressure load, ensuring the safety and stability of the container under high-pressure conditions. When the pressure within the container is high, the thinner wall thickness of the inner cylinder 112 enables efficient heat transfer and exchange. The thin-wall design reduces thermal resistance and improves heat exchange efficiency.
[0067] It should be noted that each structure is described in detail below.
[0068] It should be noted that the cylinder assembly 110 can be formed by fitting an inner cylinder 112 , an outer cylinder 111 and a central annular thick-walled circular ring.
[0069] The central, thick-walled ring not only accommodates the material inlet 113, material outlet 114, and handhole 119, but also effectively ensures the structural continuity of the jacketed portion of the cylinder or head. This design offers significant advantages at higher internal cylinder pressures, enhancing the overall stability and structural integrity of the vessel.
[0070] It should be noted that inner cylinder 112 primarily isolates the heat exchange medium from the process medium, preventing the two media from mixing and ensuring the purity and safety of the process. The process medium's pressure load is transmitted to outer cylinder 111 via the raised transfer members 120 on either side of heat exchange channel 118. The outer cylinder 111, which is nested together, bears the majority of the reaction's pressure load.
[0071] In some embodiments, the outer cylinder 111 and the inner cylinder 112 may be made of one of stainless steel, carbon steel, aluminum alloy, and titanium alloy.
[0072] Stainless steel offers excellent corrosion resistance and is suitable for handling a variety of corrosive media. Its high strength and wear resistance allow it to withstand high pressure and mechanical stress. Its smooth surface makes it easy to clean and meets hygienic requirements, making it suitable for use in the food and pharmaceutical industries. Aluminum alloy is lightweight, helping to reduce the overall weight of the equipment and facilitate transportation and installation.
[0073] Selecting corrosion-resistant materials (such as stainless steel or titanium alloy) for the outer cylinder 111 and the inner cylinder 112 can significantly extend the service life of the container and reduce the frequency of maintenance and replacement.
[0074] It should be noted that the horizontal nested container 100 provided in this application is designed to facilitate storage and transportation of liquids or gases in chemical production, where many containers are horizontal.
[0075] In some embodiments, the heat exchange channel 118 is formed by mechanical processing. The mechanical processing method can accurately control the size and shape of the heat exchange channel 118, which helps to achieve a uniform heat exchange effect and improve the heat exchange efficiency of the entire container.
[0076] Machining can generally provide a higher surface finish, reduce fluid resistance in the heat exchange channel 118 , and thus improve the flow efficiency of the heat exchange medium.
[0077] The mechanical processing method allows the design and manufacture of heat exchange channels 118 of different shapes and sizes according to specific needs. For example, the heat exchange channels 118 are arranged in a spiral shape, a serpentine shape or a broken line shape. The heat exchange channels 118 are arranged in a spiral shape to increase the heat exchange area and heat exchange efficiency to optimize the heat exchange effect.
[0078] In some optional embodiments, a material inlet 113 and a material outlet 114 are provided on the barrel assembly 110 , and both the material inlet 113 and the material outlet 114 are in communication with the accommodating chamber.
[0079] It should be noted that the arrangement of the material inlet 113 and the material outlet 114 satisfies the addition and outlet of materials.
[0080] In some embodiments, the positions and numbers of the material inlet 113 and the material outlet 114 are not particularly limited.
[0081] In some optional embodiments, a heat exchange medium inlet 115 and a heat exchange medium outlet 116 are provided on the barrel assembly 110 , and both the heat exchange medium inlet 115 and the heat exchange medium outlet 116 are communicated with the heat exchange channel 118 .
[0082] It should be noted that the arrangement of heat exchange medium inlet 115 and heat exchange medium outlet 116 enables the heat exchange medium to efficiently enter and exit heat exchange channel 118, ensuring an optimized flow path of the heat exchange medium within the channel, thereby improving heat exchange efficiency. By properly arranging heat exchange medium inlet 115 and heat exchange medium outlet 116, uniform distribution of the heat exchange medium within heat exchange channel 118 can be achieved, preventing localized overheating or overcooling and ensuring uniform heating or cooling of the material throughout the container.
[0083] A heat exchange medium inlet 115 and a heat exchange medium outlet 116 are opened on the cylinder assembly 110 and are connected to the heat exchange channel 118, which can significantly improve the heat exchange efficiency, response speed and system flexibility, while simplifying the structural design, facilitating maintenance, and having energy-saving effects and high safety.
[0084] In some optional embodiments, there are multiple transmission members 120 , and the multiple transmission members 120 are spaced apart and located between the outer cylinder 111 and the inner cylinder 112 .
[0085] It should be noted that the plurality of transmission members 120 are arranged at intervals between the outer cylinder 111 and the inner cylinder 112 , which can evenly distribute the pressure load of the process medium, reduce local stress concentration, and enhance the overall structural strength and stability of the container.
[0086] In addition, the spaced arrangement of the transmission members 120 can effectively improve the container's anti-deformation capability, prevent deformation or rupture under high pressure conditions, and ensure the safe operation of the container.
[0087] Furthermore, the design of multiple transfer members 120 can increase the contact area between the heat exchange medium and the inner cylinder 112, thereby improving heat exchange efficiency. The spaced arrangement of the transfer members 120 helps optimize the flow path of the heat exchange medium, reduce flow resistance, promote uniform flow of the heat exchange medium, and improve heat exchange efficiency.
[0088] In some optional embodiments, one end of the transmission member 120 is disposed on the inner wall of the outer cylinder 111 , and the other end of the transmission member 120 extends toward the inner cylinder 112 with a first gap between the transmission member 120 and the inner cylinder 112 .
[0089] It should be noted that one end of the transfer member 120 is fixed on the inner wall of the outer cylinder 111, and the other end extends toward the inner cylinder 112 with a first gap, which can evenly distribute the pressure load of the process medium, reduce local stress concentration, and enhance the overall structural strength and stability of the container.
[0090] The first gap between the transfer member 120 and the inner cylinder 112 helps to optimize the flow path of the heat exchange medium, reduce flow resistance, promote uniform flow of the heat exchange medium, and improve the heat exchange effect; in addition, the first gap between the transfer member 120 and the inner cylinder 112 makes maintenance and replacement more convenient, reduces maintenance time and cost, and improves the operating efficiency of the equipment.
[0091] In some optional embodiments, one end of the transmission member 120 is disposed on the outer wall of the inner cylinder 112 , and the other end of the transmission member 120 extends toward the outer cylinder 111 with a second gap between the transmission member 120 and the outer cylinder 111 .
[0092] It should be noted that multiple transfer parts 120 are designed between the outer cylinder 111 and the inner cylinder 112, and one end of the transfer part 120 is fixed on the outer wall of the inner cylinder 112, and the other end extends toward the outer cylinder 111 and leaves a second gap between the outer cylinder 111. This can significantly enhance the structural strength and stability of the container, optimize the heat exchange effect, evenly distribute thermal stress, simplify the manufacturing and maintenance process, improve safety and reliability, and flexibly adapt to different process requirements.
[0093] In some embodiments, the values of the first gap and the second gap can be adjusted according to actual conditions and are not subject to excessive restrictions.
[0094] like Figure 1 and Figure 3 As shown, in some optional embodiments, the barrel assembly 110 is provided with a stirring port 117, and the stirring port 117 is communicated with the accommodating cavity;
[0095] At least two stirring ports 117 are located on opposite sides of the barrel assembly 110 along the second direction.
[0096] It should be noted that the multiple stirring ports 117 facilitate multi-point stirring to improve the uniformity of material mixing.
[0097] In some embodiments, the stirring port 117 can be horizontally arranged on the left and right heads or vertically arranged on the central annular thick-walled ring.
[0098] Among them, such as Figure 1 As shown, Y represents the second direction.
[0099] In some optional embodiments, the material inlet 113 and the material outlet 114 are located on opposite sides of the accommodating cavity along the first direction.
[0100] It should be noted that the material inlet 113 and the outlet are located on opposite sides of the containing cavity along the first direction, which can make the material flow linearly in the containing cavity, reduce flow resistance and stagnation, and improve the flow efficiency of the material. This helps to evenly distribute the material in the containing cavity, avoids local accumulation, and ensures the uniformity and stability of the process.
[0101] As shown in Figure 1 X represents the first direction.
[0102] The linear flow of the material can ensure that the material is uniformly heated or cooled throughout the containing cavity, improving the heat exchange efficiency. This configuration can reduce the temperature gradient in the containing cavity, avoid local overheating or overcooling, and ensure the uniformity of the material temperature.
[0103] In addition, the material inlet 113 and the outlet are located on opposite sides along the first direction, which can simplify the piping design, reduce the number of connection points and potential leakage points, and improve the reliability of the system.
[0104] As shown in Figure 3 In some alternative embodiments, the horizontal nested container 100 further comprises a stirrer 130 rotating in the containing cavity.
[0105] It should be noted that the introduction of the stirrer 130 can effectively mix the material in the containing cavity, ensure the uniform distribution of the material, avoid local concentration differences, and improve the uniformity and stability of the process.
[0106] In addition, the rotation of the stirrer 130 can prevent solid particles from settling at the bottom of the containing cavity, ensuring uniform suspension of the material and improving reaction efficiency. The rotation of the stirrer 130 can increase the contact area and frequency of the material with the reaction medium, accelerate the chemical reaction, and improve the reaction rate and product quality.
[0107] In some alternative embodiments, the transmission member 120 is a fin; and / or,
[0108] The transmission member 120 is integrally formed with one of the outer cylinder 111 and the inner cylinder 112.
[0109] It should be noted that by designing the transmission member 120 as a fin and integrally forming the transmission member 120 with one of the outer cylinder 111 and the inner cylinder 112, the structural strength and stability of the container can be significantly enhanced, the heat exchange efficiency and uniformity can be improved, the manufacturing and maintenance processes can be simplified, the safety and reliability can be improved, and different process requirements can be flexibly adapted.
[0110] The horizontal nested container provided in the embodiment of the present application includes a cylinder assembly, which includes an outer cylinder and an inner cylinder. The outer cylinder is sleeved on the outer periphery of the inner cylinder, and the inner cylinder has a accommodating cavity, which is used to accommodate materials; the cylinder assembly also has a heat exchange channel, a heat exchange channel is formed between the outer cylinder and the inner cylinder, the heat exchange channel is used to inject heat exchange medium, and the heat exchange medium flows in the heat exchange channel to exchange heat with the material in the accommodating cavity; a transfer member is arranged in the heat exchange channel and is located between the outer cylinder and the inner cylinder to transfer the pressure of the inner cylinder to the outer cylinder.
[0111] The transfer elements transmit the pressure load of the process medium to the outer cylinder via the raised transfer elements on either side of the heat exchange channel on the inner cylinder. These transfer elements not only enhance the structural strength of the inner cylinder but also effectively distribute the pressure to the outer cylinder. The outer cylinder, through its sleeved structure, bears the majority of the reaction pressure load, ensuring the safety and stability of the vessel under high-pressure conditions. Even under high pressures, the thinner inner cylinder wall allows for efficient heat transfer and exchange. This thin-wall design reduces thermal resistance and improves heat exchange efficiency.
[0112] In the description of the present application, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", "clockwise", "counterclockwise", "axial", "radial", "circumferential", etc., indicating orientations or positional relationships, are based on the orientations or positional relationships shown in the accompanying drawings and are only for the convenience of describing the present application and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operate in a specific orientation, and therefore should not be understood as limiting the present application.
[0113] Furthermore, the terms "first" and "second" are used for descriptive purposes only and should not be construed as indicating or implying relative importance or implicitly specifying the number of the technical features being referred to. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one of such features. Throughout the description of this application, "plurality" means at least two, for example, two, three, etc., unless otherwise specifically defined.
[0114] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present application, rather than to limit them. Although the present application has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the aforementioned embodiments, or make equivalent replacements for some or all of the technical features therein. These modifications or replacements do not deviate the essence of the corresponding technical solutions from the scope of the technical solutions of the embodiments of the present application.
Claims
1. A horizontal nested container (100), characterized in that: include: A barrel assembly (110), the barrel assembly (110) comprising an outer barrel (111) and an inner barrel (112), the outer barrel (111) being sleeved on the outer periphery of the inner barrel (112), the inner barrel (112) having a receiving cavity, the receiving cavity being used to receive material; The barrel assembly (110) further comprises a heat exchange channel (118), wherein the heat exchange channel (118) is formed between the outer barrel (111) and the inner barrel (112), and the heat exchange channel (118) is used for injecting a heat exchange medium, and the heat exchange medium flows in the heat exchange channel (118) to perform heat exchange with the material in the accommodating cavity; A transfer member (120) is provided in the heat exchange channel (118) and is located between the outer cylinder (111) and the inner cylinder (112) to transfer the pressure of the inner cylinder (112) to the outer cylinder (111).
2. The horizontal sleeve container (100) according to claim 1, characterized in that: A material inlet (113) and a material outlet (114) are provided on the barrel assembly (110), and both the material inlet (113) and the material outlet (114) are communicated with the accommodating cavity.
3. The horizontal sleeve container (100) according to claim 1, characterized in that: A heat exchange medium inlet (115) and a heat exchange medium outlet (116) are provided on the barrel assembly (110), and both the heat exchange medium inlet (115) and the heat exchange medium outlet (116) are connected to the heat exchange channel (118).
4. The horizontal sleeve container (100) according to any one of claims 1 to 3, characterized in that: There are a plurality of transmission members (120), and the plurality of transmission members (120) are spaced apart and located between the outer cylinder (111) and the inner cylinder (112).
5. The horizontal sleeve container (100) according to any one of claims 1 to 3, characterized in that: One end of the transmission member (120) is arranged on the inner wall of the outer cylinder (111), and the other end of the transmission member (120) extends toward the inner cylinder (112) and has a first gap between the transmission member (120) and the inner cylinder (112).
6. The horizontal sleeve container (100) according to any one of claims 1 to 3, characterized in that: One end of the transmission member (120) is arranged on the outer wall of the inner cylinder (112), and the other end of the transmission member (120) extends toward the outer cylinder (111) and has a second gap with the outer cylinder (111).
7. The horizontal sleeve container (100) according to any one of claims 1 to 3, characterized in that: The barrel assembly (110) is provided with a stirring port (117), and the stirring port (117) is communicated with the accommodating cavity; At least two stirring ports (117) are located on opposite sides of the barrel assembly (110) along the second direction.
8. The horizontal sleeve container (100) according to claim 2, characterized in that: The material inlet (113) and the material outlet (114) are respectively located on opposite sides of the accommodating cavity along a first direction.
9. The horizontal sleeve container (100) according to any one of claims 1 to 3, characterized in that: The horizontal nested container (100) further comprises a stirrer (130), and the stirrer (130) is rotatably located in the accommodating cavity.
10. The horizontal sleeve container (100) according to any one of claims 1 to 3, characterized in that: The transmission member (120) is a fin; and / or, The transmission member (120) is an integrally formed structure with one of the outer cylinder (111) and the inner cylinder (112).