Hydrophobic reactor
Patent Information
- Application Number
- CN202521919122.0
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-09-05
- Publication Date
- 2026-10-09
- Estimated Expiration
- 2035-09-05
AI Technical Summary
[0003]然而，对于某些工业生产，液相反应生成物(如油、水等)随着气相产品被带出，影响气相产品的质量，或者液相反应生成物对催化反应有破坏作用，影响气相产品正常生成
[0017]由于罐体底部开设有原料入口和液相出口，顶部开设有气相出口，因此，原料可以通过原料入口进入罐体内。由于催化剂组件设于罐体内，因此，在原料经过催化剂组件时，原料会发生化学反应，以生成气相产物和液相产物，气相产物可以通过气相出口排出罐体，液相产物在重力的作用下，会落到罐体的底部。由于液相管道与液相出口连通，因此，液相产物可以通过液相管道排出。由于控制阀设于液相管道，用于控制液相管道的通断，液位计设于罐体，用于检测罐体内的液位，液位计位于催化剂组件和液相出口之间，控制器与液位计和控制阀电连接，因此，液位计可以获取液相产物在罐体内的液位值，并将液位值发送给控制器，控制器将液位值与第一设定液位值和第二设定液位值进行比较，若液位值大于第一设定液位值，则控制器控制控制阀打开，以打开液相管道，使得罐体内的液相产物可以通过液相管道排出，避免液相产物在罐体内积累过多，以避免液相产物随着气相产物被带出，保证气相产物的质量，也避免液相反应生成物对催化反应破坏，保证气相产品正常生成，若液位值小于第二设定液位值，第二设定液位值小于第一设定液位值，则控制器控制控制阀关闭，以关闭液相管道，使得罐体内的液相产物不再通过液相管道排出，以保证罐体内压力稳定，避免外部介质(如空气)反窜入罐体内，以保证气相产品正常生成，使得罐体内的液位维持在合理的范围内。
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Figure CN224822486U_ABST
Abstract
Description
Technical Field
[0001] This application belongs to the field of chemical technology, specifically relating to a hydrophobic reactor. Background Technology
[0002] In industries such as petrochemicals, fine chemicals, and pharmaceuticals, chemical reactions generally require the action of a catalyst. In most industrial reactors, a gaseous medium or a gas-liquid two-phase medium flows concurrently through the catalyst bed, generating gaseous products and liquid products.
[0003] However, in some industrial production processes, liquid-phase reaction products (such as oil and water) are carried out along with gaseous products, affecting the quality of the gaseous products, or the liquid-phase reaction products have a destructive effect on the catalytic reaction, affecting the normal generation of gaseous products. Utility Model Content
[0004] To address the aforementioned technical problems, this utility model provides a hydrophobic reactor, which aims to at least partially solve the technical problems of liquid-phase reaction products (such as oil and water) being carried out with gaseous products, affecting the quality of gaseous products, or liquid-phase reaction products having a destructive effect on catalytic reactions, affecting the normal generation of gaseous products.
[0005] The technical solution of this utility model is as follows:
[0006] A hydrophobic reactor includes: a tank body with a raw material inlet and a liquid phase outlet at the bottom and a gas phase outlet at the top; a catalyst assembly disposed within the tank body; a liquid phase pipeline connected to the liquid phase outlet; a control valve disposed within the liquid phase pipeline for controlling the opening and closing of the liquid phase pipeline; a level gauge disposed within the tank body for detecting the liquid level within the tank body, the level gauge being located between the catalyst assembly and the liquid phase outlet; and a controller electrically connected to the level gauge and the control valve.
[0007] In some embodiments, the level gauge includes: a first detection unit disposed in the tank; a second detection unit disposed in the tank; a body connected to the first detection unit and the second detection unit, and electrically connected to the controller; wherein, along the axial direction of the tank, the first detection unit and the second detection unit are spaced apart, and the first detection unit is located between the catalyst assembly and the second detection unit.
[0008] In some implementations, the raw material inlet and the liquid phase outlet are spaced apart.
[0009] In some embodiments, the hydrophobic reactor further includes a feed assembly extending through the raw material inlet and partially located within the tank body; wherein the feed assembly is located below the catalyst assembly.
[0010] In some embodiments, the feed assembly includes: a distributor disposed within the tank and located below the catalyst assembly; and a feed pipe extending through the raw material inlet and communicating with the distributor.
[0011] In some embodiments, the hydrophobic reactor further includes a gas outlet pipe connected to the gas phase outlet.
[0012] In some implementations, the vent pipe is detachably connected to the tank.
[0013] In some embodiments, the catalyst assembly includes: a first support member disposed within the tank and located between the level gauge and the gas phase outlet; and a catalyst disposed within the first support member and located between the first support member and the gas phase outlet; wherein the first support member has multiple channels.
[0014] In some implementations, the tank body is provided with a second support member, and the first support member is disposed on the second support member.
[0015] In some embodiments, the tank includes: a first sealing section having the raw material inlet and the liquid phase outlet; a second sealing section having the gas phase outlet; and a receiving section having both ends connected to the first sealing section and the second sealing section, respectively.
[0016] The beneficial effects of this utility model include at least the following:
[0017] Because the tank has a raw material inlet and a liquid phase outlet at the bottom, and a gas phase outlet at the top, raw materials can enter the tank through the raw material inlet. Since the catalyst assembly is located inside the tank, the raw material undergoes a chemical reaction as it passes through the catalyst assembly, generating gaseous and liquid phase products. The gaseous products can be discharged from the tank through the gas phase outlet, while the liquid phase products fall to the bottom of the tank under gravity. Because the liquid phase pipeline is connected to the liquid phase outlet, the liquid phase products can be discharged through the liquid phase pipeline. Because the control valve is located in the liquid phase pipeline to control its opening and closing, and the level gauge is located in the tank to detect the liquid level inside the tank, the level gauge is situated between the catalyst assembly and the liquid phase outlet. The controller is electrically connected to the level gauge and the control valve. Therefore, the level gauge can obtain the liquid level value of the liquid phase product in the tank and send it to the controller. The controller compares the liquid level value with a first set liquid level value and a second set liquid level value. If the liquid level value is greater than the first set liquid level value, the controller controls the control valve to open, thereby opening the liquid phase pipeline and allowing the liquid phase product in the tank to be discharged through the liquid phase pipeline, preventing the liquid phase from being discharged. Excessive accumulation of product within the tank is prevented to avoid the liquid phase product being carried out along with the gas phase product, ensuring the quality of the gas phase product and preventing the liquid phase reaction products from damaging the catalytic reaction, thus ensuring the normal generation of the gas phase product. If the liquid level is lower than the second set liquid level value, and the second set liquid level value is lower than the first set liquid level value, the controller will close the control valve to shut off the liquid phase pipeline, preventing the liquid phase product in the tank from being discharged through the liquid phase pipeline, thus ensuring stable pressure in the tank and preventing external media (such as air) from backflowing into the tank, ensuring the normal generation of the gas phase product, and maintaining the liquid level in the tank within a reasonable range. Attached Figure Description
[0018] To more clearly illustrate the technical solutions in the embodiments of this application, the accompanying drawings used in the description of the embodiments will be briefly introduced below. Obviously, the accompanying drawings described below are some embodiments of this application. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.
[0019] Figure 1 This is a schematic diagram of the structure of a hydrophobic reactor in some embodiments.
[0020] In the attached image:
[0021] Tank body 10, raw material inlet 11, liquid phase outlet 12, gas phase outlet 13, first sealing part 14, second sealing part 15, and containment part 16;
[0022] Catalyst assembly 20, first support 21, catalyst 22, second support 23;
[0023] Liquid phase pipeline 30;
[0024] Control valve 40;
[0025] Level gauge 50, first detection unit 51, second detection unit 52, body 53;
[0026] Feed assembly 60, distributor 61, feed pipe 62;
[0027] Air outlet 70. Detailed Implementation
[0028] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.
[0029] It should be noted that all directional indications in this utility model embodiment are only used to explain the relative positional relationship and movement of each component in a specific posture. If the specific posture changes, the directional indications will also change accordingly.
[0030] In this utility model, unless otherwise explicitly specified and limited, the terms "connection," "fixing," etc., should be interpreted broadly. For example, "fixing" can mean a fixed connection, a detachable connection, or an integral part; it can mean a mechanical connection or an electrical connection; it can mean a direct connection or an indirect connection through an intermediate medium; it can mean the internal communication of two components or the interaction between two components, unless otherwise explicitly limited. Those skilled in the art can understand the specific meaning of the above terms in this utility model according to the specific circumstances.
[0031] Furthermore, in this utility model, descriptions involving "first," "second," etc., are for descriptive purposes only and should not be construed as indicating or implying their relative importance or implicitly specifying the number of technical features indicated. Therefore, a feature defined with "first" or "second" may explicitly or implicitly include at least one of that feature. Additionally, the technical solutions of the various embodiments can be combined with each other, but only on the basis of being achievable by those skilled in the art. When the combination of technical solutions is contradictory or impossible to implement, such a combination of technical solutions should be considered non-existent and not within the scope of protection claimed by this utility model.
[0032] This application is described below with reference to the accompanying drawings and specific embodiments:
[0033] The hydrophobic reactor provided in this application aims to at least partially solve the technical problems of liquid-phase reaction products (such as oil, water, etc.) being carried out with gaseous products, affecting the quality of gaseous products, or liquid-phase reaction products having a destructive effect on catalytic reactions, affecting the normal generation of gaseous products.
[0034] Figure 1 This is a schematic diagram of the structure of a hydrophobic reactor according to some embodiments. (Combined with...) Figure 1 The hydrophobic reactor in this embodiment includes: a tank 10, a catalyst assembly 20, a liquid phase pipeline 30, a control valve 40, a level gauge 50, and a controller (not shown in the figure). The tank 10 has a raw material inlet 11 and a liquid phase outlet 12 at the bottom, and a gas phase outlet 13 at the top. The catalyst assembly 20 is disposed inside the tank 10. The liquid phase pipeline 30 is connected to the liquid phase outlet 12. The control valve 40 is disposed in the liquid phase pipeline 30 and is used to control the opening and closing of the liquid phase pipeline 30. The level gauge 50 is disposed in the tank 10 and is used to detect the liquid level inside the tank 10; the level gauge 50 is located between the catalyst assembly 20 and the liquid phase outlet 12. The controller is electrically connected to the level gauge 50 and the control valve 40.
[0035] Since the tank 10 has a raw material inlet 11 and a liquid phase outlet 12 at the bottom and a gas phase outlet 13 at the top, the raw material can enter the tank 10 through the raw material inlet 11. Because the catalyst assembly 20 is located inside the tank 10, the raw material undergoes a chemical reaction when passing through the catalyst assembly 20, generating gaseous and liquid phase products. The gaseous products can be discharged from the tank 10 through the gas phase outlet 13, while the liquid phase products fall to the bottom of the tank 10 under gravity. Since the liquid phase pipe 30 is connected to the liquid phase outlet 12, the liquid phase products can be discharged through the liquid phase pipe 30. Since the control valve 40 is located in the liquid phase pipeline 30 to control the opening and closing of the liquid phase pipeline 30, and the level gauge 50 is located in the tank 10 to detect the liquid level in the tank 10, the level gauge 50 is located between the catalyst assembly 20 and the liquid phase outlet 12. The controller is electrically connected to the level gauge 50 and the control valve 40. Therefore, the level gauge 50 can obtain the liquid level value of the liquid phase product in the tank 10 and send the liquid level value to the controller. The controller compares the liquid level value with a first set liquid level value and a second set liquid level value. If the liquid level value is greater than the first set liquid level value, the controller controls the control valve 40 to open, thereby opening the liquid phase pipeline 30, so that the liquid phase product in the tank 10 can pass through the liquid phase pipeline. The liquid phase product is discharged through the liquid phase pipe 30 to prevent excessive accumulation of liquid phase products in the tank 10. This is to prevent the liquid phase products from being carried out with the gas phase products, ensuring the quality of the gas phase products and preventing the liquid phase reaction products from damaging the catalytic reaction. This ensures the normal generation of gas phase products. If the liquid level is lower than the second set liquid level value, and the second set liquid level value is lower than the first set liquid level value, the controller controls the control valve 40 to close, thereby closing the liquid phase pipe 30. This prevents the liquid phase products in the tank 10 from being discharged through the liquid phase pipe 30, ensuring stable pressure in the tank 10 and preventing external media (such as air) from backflowing into the tank 10. This ensures the normal generation of gas phase products and keeps the liquid level in the tank 10 within a reasonable range.
[0036] Combination Figure 1 In some embodiments, to detect the liquid level of the liquid product inside the tank 10, the level gauge 50 includes a first detection unit 51, a second detection unit 52, and a body 53. The first detection unit 51 is disposed in the tank 10. The second detection unit 52 is disposed in the tank 10. The body 53 is connected to the first detection unit 51 and the second detection unit 52, and is electrically connected to a controller. The first detection unit 51 and the second detection unit 52 are spaced apart along the axial direction of the tank 10, with the first detection unit 51 located between the catalyst assembly 20 and the second detection unit 52.
[0037] The second detection unit 52 is located below the first detection unit 51. When the liquid product in the tank 10 reaches the first detection unit 51, the first detection unit 51 sends the liquid level value to the main body 53, which in turn sends the liquid level value to the controller. The controller compares the liquid level value detected by the first detection unit 51 with a first set liquid level value. If the liquid level value detected by the first detection unit 51 is greater than the first set liquid level value, the controller controls the control valve 40 to open, thereby opening the liquid phase pipeline 30. This allows the liquid product in the tank 10 to be discharged through the liquid phase pipeline 30, preventing excessive accumulation of liquid product in the tank 10. This avoids the liquid product being carried out with the gaseous product, ensuring the quality of the gaseous product, and also preventing the liquid reaction products from damaging the catalytic reaction, thus ensuring the normal generation of the gaseous product. As the liquid phase product is discharged from the liquid phase pipeline 30, the liquid phase product level in the tank 10 will drop. When the liquid phase product in the tank 10 reaches the second detection unit 52, the second detection unit 52 sends the liquid level value to the main body 53, and the main body 53 sends the liquid level value to the controller. The controller compares the liquid level value detected by the second detection unit 52 with the second set liquid level value. If the liquid level value detected by the second detection unit 52 is less than the second set liquid level value, and the second set liquid level value is less than the first set liquid level value, the controller controls the control valve 40 to close, thereby closing the liquid phase pipeline 30. This prevents the liquid phase product in the tank 10 from being discharged through the liquid phase pipeline 30, ensuring stable pressure in the tank 10 and preventing external media (such as air) from backflowing into the tank 10, thus ensuring the normal generation of the gas phase product.
[0038] In some embodiments, the main body 53 is provided with a display screen to display the liquid level of the liquid product in the tank 10, so that the staff can know the liquid level of the liquid product in the tank 10.
[0039] Combination Figure 1 In some embodiments, in order to ensure that the raw materials can fully reach the catalyst assembly 20, the raw material inlet 11 and the liquid phase outlet 12 are spaced apart to prevent the raw materials from being discharged from the liquid phase outlet 12, and to ensure that the raw materials can fully contact the catalyst assembly 20, thereby improving the reaction efficiency.
[0040] In some embodiments, for conveying raw materials into the tank 10, the hydrophobic reactor further includes a feed assembly 60. The feed assembly 60 passes through the raw material inlet 11 and is partially located inside the tank 10. The feed assembly 60 is located below the catalyst assembly 20.
[0041] Raw materials can enter the tank 10 through the feed assembly 60. The raw materials will reach the catalyst assembly 20. When the raw materials pass through the catalyst assembly 20, the raw materials will undergo a chemical reaction to generate gaseous products and liquid products.
[0042] Combination Figure 1In some embodiments, to ensure uniform distribution of raw materials, the feeding assembly 60 includes a distributor 61 and a feed pipe 62. The distributor 61 is located inside the tank 10 and below the catalyst assembly 20. The feed pipe 62 passes through the raw material inlet 11 and communicates with the distributor 61.
[0043] The raw material enters the distributor 61 through the feed pipe 62. The distributor 61 distributes the raw material so that it can be evenly distributed on the cross-section of the tank 10, so that the raw material can fully contact the catalyst assembly 20 and achieve a full reaction.
[0044] Combination Figure 1 In some embodiments, the hydrophobic reactor further includes an outlet pipe 70 for discharging the gaseous products. The outlet pipe 70 is connected to the gas phase outlet 13, and the gaseous products generated after the raw materials react with the catalyst assembly 20 can enter the outlet pipe 70 through the gas phase outlet 13, and the gaseous products are transported to the receiving point through the outlet pipe 70.
[0045] In some embodiments, to achieve multiple uses for the gas phase outlet 13, the gas outlet pipe 70 is detachably connected to the tank 10. It is understood that when gas phase products need to be discharged, the gas outlet pipe 70 is connected to the tank 10 and the gas phase outlet 13 is connected. The gas phase products generated after the raw materials react with the catalyst assembly 20 can enter the gas outlet pipe 70 through the gas phase outlet 13 and be transported to the storage location through the gas outlet pipe 70. When the equipment inside the tank 10 needs to be repaired, the gas outlet pipe 70 is removed from the tank 10. At this time, the gas phase outlet 13 can be used as a maintenance port. The staff can repair the equipment inside the tank 10 through the maintenance port without having to drill holes in the tank 10. This achieves multiple uses for the gas phase outlet 13 and reduces processing costs.
[0046] Combination Figure 1 In some embodiments, to enable the raw materials to react within the catalyst assembly 20, the catalyst assembly 20 includes a first support 21 and a catalyst 22. The first support 21 is disposed within the tank 10 and located between the level gauge 50 and the gas phase outlet 13. The catalyst 22 is disposed within the first support 21 and located between the first support and the gas phase outlet 13. The first support 21 has multiple channels.
[0047] In some embodiments, the catalyst 22 is supported by the first support member 21. After the raw material enters the tank 10, the raw material enters the catalyst 22 through multiple channels, so that the raw material can react in the catalyst 22 to generate liquid phase products and gas phase products.
[0048] In some embodiments, the catalyst can be a molecular sieve catalyst for catalytic cracking. For catalytic reforming, the catalyst can be a noble metal catalyst. For hydrogen production, the catalyst can be a nickel-based catalyst.
[0049] In some embodiments, the area of the catalyst assembly 20 is matched with the cross-sectional area of the tank 10.
[0050] Combination Figure 1 In some embodiments, in order to ensure the stability of the installation of the first support member 21, a second support member 23 is provided inside the tank body 10. The first support member 21 is located on the second support member 23, and the second support member 23 supports the first support member 21 to prevent the first support member 21 from falling off, so as to ensure that the raw materials can react normally in the catalyst 22.
[0051] In some embodiments, to prevent the second support 23 from blocking the raw material from entering the catalyst 22, the second support 23 may be annular, allowing the raw material to pass through. Of course, in other embodiments, the second support 23 may consist of multiple spaced-apart support portions, allowing the raw material to enter the catalyst 22.
[0052] In some embodiments, in order to ensure that the raw materials can enter the catalyst 22, the first support member 21 includes a grid, with two adjacent grids spaced apart, and the gap between the two grids forming a channel, so that the raw materials can enter the catalyst 22 through the channel, thereby ensuring that the raw materials can react normally in the catalyst 22.
[0053] In some embodiments, after the catalyst 22 is deposited on the first support 22, the catalyst 22 has voids that allow the raw materials, gaseous products and liquid products to flow through the voids, so as to ensure that the reaction of the raw materials can proceed normally.
[0054] Combination Figure 1 In some embodiments, to prevent leakage of raw materials, gaseous products, and liquid products, the tank 10 includes a first sealing section 14, a second sealing section 15, and a receiving section 16. The first sealing section 14 has a raw material inlet 11 and a liquid outlet 12. The second sealing section 15 has a gas outlet 13. The receiving section 16 is connected at both ends to the first sealing section 14 and the second sealing section 15, respectively.
[0055] The first sealing part 14 and the second sealing part 15 respectively seal both ends of the receiving part 16 to prevent leakage of raw materials, gaseous products and liquid products.
[0056] In some embodiments, the first sealing portion 14 and the second sealing portion 15 may be hemispherical heads or elliptical heads.
[0057] In some embodiments, the tank 10 is installed vertically. A skirt support can be provided at the bottom of the tank 10 to support the tank 10, or an ear support can be provided on the side of the tank to install it to the frame.
[0058] In the description of this application, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are used only for the convenience of describing this application and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this application.
[0059] In the description of this utility model, unless otherwise expressly specified and limited, "above" or "below" the second feature can include direct contact between the first and second features, or contact between the first and second features through another feature between them. Furthermore, "above," "over," and "on top" of the second feature includes the first feature directly above or diagonally above the second feature, or simply indicates that the first feature is at a higher horizontal level than the second feature. "Below," "below," and "under" the second feature includes the first feature directly below or diagonally below the second feature, or simply indicates that the first feature is at a lower horizontal level than the second feature.
[0060] In the description of this specification, the references to terms such as "one embodiment," "some embodiments," "example," "specific example," or "some examples," etc., indicate that a specific feature, structure, material, or characteristic described in connection with that embodiment or example is included in at least one embodiment or example of this application. In this specification, the illustrative expressions of the above terms do not necessarily refer to the same embodiment or example. Furthermore, the specific features, structures, materials, or characteristics described may be combined in any suitable manner in one or more embodiments or examples. In addition, those skilled in the art can combine and integrate the different embodiments or examples described in this specification.
[0061] Although preferred embodiments of this application have been described, those skilled in the art, upon learning the basic inventive concept, can make other changes and modifications to these embodiments. Therefore, the appended claims are intended to be interpreted as including the preferred embodiments as well as all changes and modifications falling within the scope of this application.
[0062] Obviously, those skilled in the art can make various modifications and variations to this application without departing from the spirit and scope of this application. Therefore, if such modifications and variations fall within the scope of the claims of this application and their equivalents, this application also intends to include such modifications and variations.
Claims
1. A hydrophobic reactor, characterized in that, include: The tank has a raw material inlet and a liquid outlet at the bottom, and a gas outlet at the top; The catalyst assembly is disposed within the tank. A liquid phase pipeline is connected to the liquid phase outlet; A control valve is located in the liquid phase pipeline and is used to control the opening and closing of the liquid phase pipeline; A level gauge is installed in the tank to detect the liquid level inside the tank. The level gauge is located between the catalyst assembly and the liquid phase outlet. The controller is electrically connected to the level gauge and the control valve.
2. The hydrophobic reactor according to claim 1, characterized in that, The level gauge includes: The first detection unit is located in the tank. The second detection unit is located in the tank. The main body is connected to the first detection unit and the second detection unit, and is electrically connected to the controller; Along the axial direction of the tank, the first detection unit and the second detection unit are spaced apart, with the first detection unit located between the catalyst assembly and the second detection unit.
3. The hydrophobic reactor according to claim 1, characterized in that, The raw material inlet and the liquid phase outlet are spaced apart.
4. The hydrophobic reactor according to any one of claims 1-3, characterized in that, The hydrophobic reactor also includes: A feeding assembly is installed through the raw material inlet and partially located inside the tank; The feed assembly is located below the catalyst assembly.
5. The hydrophobic reactor according to claim 4, characterized in that, The feeding assembly includes: A distributor is disposed inside the tank and located below the catalyst assembly; A feed pipe is installed at the raw material inlet and is connected to the distributor.
6. The hydrophobic reactor according to any one of claims 1-3, characterized in that, The hydrophobic reactor also includes: The gas outlet pipe is connected to the gas phase outlet.
7. The hydrophobic reactor according to claim 6, characterized in that, The vent pipe is detachably connected to the tank.
8. The hydrophobic reactor according to any one of claims 1-3, characterized in that, The catalyst assembly includes: A first support member is disposed inside the tank and located between the level gauge and the gas phase outlet; The catalyst is disposed on the first support and located between the first support and the gas phase outlet; The first support member has multiple channels.
9. The hydrophobic reactor according to claim 8, characterized in that, The tank body is provided with a second support member, and the first support member is disposed on the second support member.
10. The hydrophobic reactor according to any one of claims 1-3, characterized in that, The tank includes: The first sealing section has the raw material inlet and the liquid phase outlet; The second sealing section has the aforementioned gas phase outlet; The receiving part is connected at both ends to the first sealing part and the second sealing part, respectively.