A natural gas deacidification device

Abstract

The invention discloses a natural gas deacidification device, including a deacidification tower and a separation cylinder, wherein two transverse tubes are rotatably connected inside the deacidification tower, and multiple stirring tubes are fixedly connected to the surfaces of the two transverse tubes, and multiple air outlets are arranged on the surfaces of the multiple stirring tubes, and a rotating mechanism for rotating the two transverse tubes is arranged on the surface of the deacidification tower; the separation cylinder is fixedly connected to the top of the upper connection box, and a conical baffle is arranged at the center of the bottom of the separation cylinder, and a wiper mechanism for the conical baffle is arranged inside the deacidification tower, and a water vapor separation mechanism is arranged inside the separation cylinder. The present invention can facilitate the full mixing of the internal natural gas and the internal solution during use through the mutual coordination of the two transverse tubes and the multiple stirring tubes, so as to facilitate the deacidification of the natural gas, and at the same time, the solvent inside the deacidification tower is circulated and heated to release the acidic gas inside the solvent, so that the solvent can be recycled, and the surface of the refrigerator is also cooled, so as to improve the use effect of the device.

Description

Technical Field

[0001] This invention relates to the field of natural gas processing technology, and more particularly to a natural gas deacidification device. Background Technology

[0002] Natural gas is a gas primarily composed of hydrocarbons such as methane. It is a clean and efficient fossil fuel, commonly used in power generation, heating, industrial production, and transportation. Vast natural gas resources are stored in underground rock formations. Through extraction, purification, and transportation, natural gas can be extracted from the ground and supplied to people. Natural gas has advantages such as high calorific value, low emissions, and ease of storage and transportation, thus playing an important role in the global energy structure. Natural gas deacidification refers to the process of removing acidic components from natural gas. These acidic components are mainly hydrogen sulfide and sulfur dioxide, as well as other sulfides and oxides. The purpose of deacidification is to reduce the content of acidic substances in natural gas to avoid corrosion of pipelines and equipment, while also improving the quality and utilization value of natural gas.

[0003] The amine process is a commonly used gas deacidification process suitable for natural gas containing acidic gases such as carbon dioxide and hydrogen sulfide. This process utilizes an amine solution to absorb the acidic gases, separating them from the natural gas through physical absorption and chemical reactions. However, most existing natural gas deacidification devices mix the natural gas with the amine solution to allow the solution to fuse the acidic gases. In practice, however, the mixing of natural gas and amine solution is often insufficient, resulting in a relatively poor deacidification effect. Furthermore, some moisture may mix with the natural gas during operation, further complicating the treatment process. Additionally, the amine solution accumulates more acidic gases over time, reducing its effectiveness and necessitating frequent replacement, thus diminishing the overall performance of the natural gas deacidification device. Summary of the Invention

[0004] Based on the technical problems existing in the background technology, the present invention proposes a natural gas deacidification device.

[0005] This invention proposes a natural gas deacidification device, comprising a deacidification tower and a separation cylinder. The deacidification tower has an upper connecting box and a lower connecting box fixedly connected to its upper and lower ends, respectively. Two horizontal pipes are rotatably connected inside the deacidification tower, both horizontally arranged. Multiple stirring tubes are fixedly connected to the surface of each of the two horizontal pipes, and multiple gas outlet holes are provided on the surface of each stirring tube. A rotating mechanism for rotating the two horizontal pipes is provided on the surface of the deacidification tower. The separation cylinder is fixedly connected to the top of the upper connecting box and communicates with the interior of the deacidification tower. A discharge pipe is fixedly connected to the center of the top of the separation cylinder and communicates with the interior of the separation cylinder. A conical baffle is provided at the center of the bottom inside the separation cylinder, and the surface of the conical baffle is fixedly connected to… The system is equipped with multiple support rods, which are evenly distributed in a ring. One end of each support rod is fixedly connected to the inner wall of the separation cylinder. The deacidification tower is equipped with a scraping mechanism for the conical baffles, and the separation cylinder is equipped with a water vapor separation mechanism. Through the cooperation of two horizontal pipes and multiple stirring pipes, the natural gas delivered to the deacidification tower can be fully mixed with the solution inside during use, thereby facilitating the deacidification of the natural gas. At the same time, the solvent inside the deacidification tower is circulated and heated to release the acidic gas inside the solvent, allowing the solvent to be recycled. Simultaneously, the surface of the cooler is cooled, allowing the deacidified natural gas to be dehydrated again, thereby improving the efficiency of the device.

[0006] Preferably, the rotating mechanism includes gears, with a connecting shaft fixedly connected to one end of each of the two horizontal tubes. Each of the two connecting shafts is sleeved inside the deacidification tower at one end. Two gears are provided, each fixedly connected to one end of a connecting shaft and meshing with it. A side plate is fixedly connected to the surface of the deacidification tower near the two gears, and the side plate is disposed on the surface of the two gears. A reduction motor is mounted on the surface of the side plate, and the output shaft of the reduction motor is fixedly connected to the center of one of the gear surfaces. Two rotating... The connector has two horizontal pipes, one end of which is installed on one end of two rotary joints. The deacidification tower has a feed pipe at the end away from the two gears. The feed pipe is horizontally positioned and has two feed branch pipes fixedly connected to one end. The two feed branch pipes are installed at the other end of the two rotary joints. Valves are installed on the surface of the two feed branch pipes to drive the two horizontal pipes and multiple stirring pipes on the surface to rotate, thereby creating a stirring effect at the bottom of the deacidification tower and fully mixing the natural gas delivered to the deacidification tower, thus improving the deacidification effect of the natural gas.

[0007] Furthermore, the scraping mechanism includes scrapers, a rotating shaft is vertically rotatably connected inside the deacidification tower, a first horizontal plate and a second horizontal plate are provided inside the deacidification tower, both of which are horizontally arranged, the bottom end of the rotating shaft is rotatably connected to the top of the first horizontal plate, the rotating shaft is sleeved inside the second horizontal plate, the top end of the rotating shaft is rotatably connected to the center of the bottom of the conical baffle, a worm gear is sleeved on the surface of the rotating shaft, and a worm is sleeved on the surface of one of the horizontal pipes, the worm gear and the worm cooperate with each other, two scrapers are provided, both scrapers are rotatably connected to the bottom of the conical baffle, both scraper surfaces are fixedly connected to connecting rods, and both connecting rods are fixedly connected to the surface of the rotating shaft. The conical baffle is used to block the moisture inside the natural gas when it passes through after deacidification, thereby reducing the moisture content inside the natural gas. During use, both scrapers can be rotated simultaneously, which facilitates the removal of water vapor at the bottom of the conical baffle, thereby better dehydrating the natural gas.

[0008] Preferably, the water vapor separation mechanism includes a cooler. A fixed box is fixedly connected to the arc surface of the separation cylinder, and the fixed box is connected to the interior of the separation cylinder. The cooler is installed inside the fixed box. A condensing plate is fixedly connected inside the separation cylinder. The condensing plate is circular and fits against the inner wall of the separation cylinder. The condensing plate is installed on the surface of the cooler. Multiple heat sinks are arranged vertically inside the fixed box and are installed on the surface of the cooler. The upper and lower ends of the fixed box are conical. An exhaust pipe is fixedly connected to the top of the fixed box. The cooler cools the condensing plate, and when natural gas passes through, the moisture inside the natural gas condenses on the surface of the condensing plate, thereby reducing the moisture content of the natural gas and improving the treatment effect of the natural gas.

[0009] Furthermore, a first connecting pipe is fixedly connected to the center of the bottom of the lower connecting box. A first suction pump is installed at one end of the first connecting pipe and is located at the bottom of the deacidification tower. A second connecting pipe is installed on the surface of the first suction pump, and the top end of the second connecting pipe is located on the surface of the fixed box. The connection between the second connecting pipe and the fixed box is located at the top of multiple heat sinks. Fixed plates are horizontally fixedly connected to both sides of the surface of the deacidification tower. Support frames are fixedly connected to the surfaces of both fixed plates. A first fixing member is fixedly connected to the surface of one of the fixed plates, and the second connecting pipe is sleeved inside the first fixing member. A cooling box is located on the side of the surface of the deacidification tower away from the first suction pump. A collecting pipe is fixedly connected to the surface of the cooling box and communicates with the interior of the cooling box. The top end of the collecting pipe is fixedly connected to the center of the bottom of the fixed box. A second suction pump is located on the side of the surface of the deacidification tower away from the first suction pump. A pump is positioned between the deacidification tower and the cooling box. A third and fourth connecting pipe are mounted on the surface of the second suction pump. One end of the fourth connecting pipe is fixedly connected to the surface of the cooling box and communicates with the interior of the cooling box. Two spray pipes are installed inside the deacidification tower, both horizontally positioned at the top of two horizontal pipes. Multiple spray heads are installed at the bottom of each spray pipe. One end of each spray pipe is inserted through one side of the deacidification tower surface and is fixedly connected to the same connecting branch pipe. The top of the third connecting pipe is fixedly connected to the surface of the connecting branch pipe. This third connecting pipe circulates the solvent at the bottom of the deacidification tower and simultaneously transports the solvent to the fixed box, passing between multiple heat sinks on the cooler. This cools the heat generated by the cooler during operation and simultaneously heats the solvent, making it easier for the acidic gases inside to evaporate.

[0010] In this invention, the natural gas requiring deacidification can be connected to one end of the feed pipe via a pipeline. Then, the valves on the surfaces of the two feed branch pipes are opened, allowing the gas requiring deacidification to be transported through the two feed branch pipes and the two valves into the two horizontal pipes. Subsequently, the geared motor is driven, and the two horizontal pipes rotate simultaneously under the connection of two gears. Then, under the action of multiple stirring pipes, the natural gas requiring deacidification is transported into the deacidification tower and can be mixed with the solvent inside the deacidification tower. At the same time, the rotation of the two horizontal pipes and multiple stirring pipes makes the natural gas and solvent transported into the deacidification tower more thoroughly mixed.

[0011] At the same time, the worm gear will drive the worm wheel to rotate, and through the connection of the rotating shaft and the two connecting rods, the two scrapers will scrape away the water at the bottom of the conical baffle.

[0012] The first suction pump drives the solvent at the bottom of the deacidification tower to be transported to the fixed box through the first and second connecting pipes. Under the action of multiple heat sinks, the solvent machine is heated. After the solvent is heated, the acidic gas inside the solvent is released, and the multiple heat sinks are cooled down at the same time.

[0013] The cooling tank can cool the solvent, and the second suction pump can transport the solvent inside the cooling tank to the two connecting branches through the third connecting pipe and the connecting branch pipe. The solvent is then sprayed out through multiple spray nozzles, thereby circulating the solvent and improving the effectiveness of the device. Attached Figure Description

[0014] Figure 1 This is a front view of a natural gas deacidification device proposed in this invention;

[0015] Figure 2 This is a schematic diagram of the surface structure of a natural gas deacidification device proposed in this invention;

[0016] Figure 3 This is a cross-sectional view of the internal structure of a natural gas deacidification device proposed in this invention;

[0017] Figure 4 for Figure 3 Enlarged view of point A;

[0018] Figure 5 This is a schematic diagram of the rotating mechanism of a natural gas deacidification device proposed in this invention;

[0019] Figure 6 This is a schematic diagram of the scraping mechanism of a natural gas deacidification device proposed in this invention;

[0020] Figure 7 This is a schematic diagram of the water vapor separation mechanism of a natural gas deacidification device proposed in this invention;

[0021] Figure 8 This is a schematic diagram of the surface structure of a natural gas deacidification device proposed in this invention.

[0022] In the diagram: 1. Deacidification tower; 11. Upper connecting box; 12. Lower connecting box; 13. Fixing plate; 14. Support frame; 15. First fixing component; 16. Side plate; 17. First horizontal plate; 18. Second horizontal plate; 2. Separation cylinder; 21. Conical baffle; 22. Support rod; 23. Discharge pipe; 3. Fixing box; 31. Exhaust pipe; 4. Cooling box; 41. Collection pipe; 5. Feed pipe; 51. Feed branch pipe; 52. Valve; 53. Rotary joint; 6. First extraction tube. Suction pump; 61. First connecting pipe; 62. Second connecting pipe; 7. Horizontal pipe; 71. Stirring pipe; 72. Air outlet; 73. Gear; 74. Gearbox; 75. Worm gear; 8. Refrigerator; 81. Condensing plate; 82. Heat sink; 9. Second suction pump; 91. Third connecting pipe; 92. Connecting branch pipe; 93. Spray pipe; 94. Spray head; 95. Fourth connecting pipe; 100. Rotating shaft; 101. Worm gear; 102. Scraper; 103. Connecting rod. Detailed Implementation

[0023] The technical solutions of the present invention will be clearly and completely described below with reference to the accompanying drawings of the embodiments of the present invention. Obviously, the described embodiments are only some embodiments of the present invention, and not all embodiments.

[0024] Reference Figures 1-8 A natural gas deacidification device includes a deacidification tower 1 and a separation cylinder 2. The deacidification tower 1 has an upper connecting box 11 and a lower connecting box 12 fixedly connected to its upper and lower ends, respectively. Two horizontal pipes 7 are rotatably connected inside the deacidification tower 1. Both horizontal pipes 7 are horizontally arranged, and multiple stirring tubes 71 are fixedly connected to the surface of each horizontal pipe 7. Multiple gas outlet holes 72 are provided on the surface of each stirring tube 71. A rotating mechanism for rotating the two horizontal pipes 7 is provided on the surface of the deacidification tower 1. The separation cylinder 2 is fixedly connected to the top of the upper connecting box 11 and communicates with the interior of the deacidification tower 1. A discharge pipe 23 is fixedly connected to the center of the top of the separation cylinder 2 and communicates with the interior of the separation cylinder 2. A conical baffle 21 is provided at the center of the bottom inside the separation cylinder 2, and a conical baffle 21 is fixedly connected to the surface of the conical baffle 21. Multiple support rods 22 are evenly distributed in a ring, with one end of each support rod 22 fixedly connected to the inner wall of the separation cylinder 2. The deacidification tower 1 is equipped with a scraping mechanism for the conical baffle 21, and the separation cylinder 2 is equipped with a water vapor separation mechanism. Through the cooperation of two horizontal pipes 7 and multiple stirring pipes 71, the natural gas delivered to the deacidification tower 1 can be fully mixed with the solution inside during use, thus facilitating the deacidification of the natural gas. At the same time, the solvent inside the deacidification tower 1 is circulated and heated to release the acidic gas inside the solvent, allowing the solvent to be recycled. Simultaneously, the surface of the cooler 8 is cooled, allowing the deacidified natural gas to be dehydrated again, thereby improving the efficiency of the device.

[0025] Reference Figure 2 , Figure 3 , Figure 4 and Figure 5 In a preferred embodiment, the rotating mechanism includes gears 73. Two horizontal tubes 7 are each fixedly connected to one end of a connecting shaft, and both connecting shafts are sleeved inside the deacidification tower 1. Two gears 73 are provided, each fixedly connected to one end of a connecting shaft and meshing with it. A side plate 16 is fixedly connected to the surface of the deacidification tower 1 near the two gears 73. The side plate 16 is disposed on the surface of the two gears 73, and a reduction motor 74 is mounted on the surface of the side plate 16. The output shaft of the reduction motor 74 is fixedly connected to the center of the surface of one of the gears 73. Two rotary gears are mounted on the surface of the deacidification tower 1 away from the two gears 73. The adapter 53 has two horizontal pipes 7, the other ends of which are respectively installed on one end of the two rotary joints 53. The deacidification tower 1 is provided with a feed pipe 5 at the end away from the two gears 73. The feed pipe 5 is horizontally arranged. One end of the feed pipe 5 is fixedly connected to two feed branch pipes 51. One end of the two feed branch pipes 51 is respectively installed on the other end of the two rotary joints 53. Valves 52 are installed on the surface of the two feed branch pipes 51 to drive the two horizontal pipes 7 and the multiple stirring pipes 71 on the surface to rotate, thereby creating a stirring effect at the bottom of the deacidification tower 1 and fully mixing the natural gas delivered to the deacidification tower 1, thereby improving the deacidification effect of the natural gas.

[0026] Reference Figure 3 , Figure 5 and Figure 6 In a preferred embodiment, the scraping mechanism includes a scraper 102. A rotating shaft 100 is vertically rotatably connected inside the deacidification tower 1. A first horizontal plate 17 and a second horizontal plate 18 are arranged inside the deacidification tower 1, both of which are horizontally arranged. The bottom end of the rotating shaft 100 is rotatably connected to the top of the first horizontal plate 17. The rotating shaft 100 is sleeved inside the second horizontal plate 18. The top end of the rotating shaft 100 is rotatably connected to the center of the bottom of the conical baffle 21. A worm gear 101 is sleeved on the surface of the rotating shaft 100. A worm 75 is sleeved on the surface of one of the horizontal pipes 7. The worm gear 101 and the worm 75 are connected to each other. 5. Two scrapers 102 are provided, both of which are rotatably connected to the bottom of the conical baffle 21. Connecting rods 103 are fixedly connected to the surfaces of both scrapers 102, and both connecting rods 103 are fixedly connected to the surfaces of the rotating shaft 100. The conical baffle 21 blocks the moisture inside the natural gas as it passes through after deacidification, thereby reducing the moisture content inside the natural gas. During use, both scrapers 102 can be rotated simultaneously, which facilitates the removal of water vapor at the bottom of the conical baffle 21, thus better dehydrating the natural gas.

[0027] Reference Figure 6 and Figure 7In a preferred embodiment, the water vapor separation mechanism includes a cooler 8. A fixed box 3 is fixedly connected to the arc surface of the separation cylinder 2, and the fixed box 3 is connected to the interior of the separation cylinder 2. The cooler 8 is installed inside the fixed box 3. A condensing plate 81 is fixedly connected inside the separation cylinder 2. The condensing plate 81 is circular and fits against the inner wall of the separation cylinder 2. The condensing plate 81 is installed on the surface of the cooler 8. Multiple heat sinks 82 are arranged vertically inside the fixed box 3 and are installed on the surface of the cooler 8. The upper and lower ends of the fixed box 3 are conical. An exhaust pipe 31 is fixedly connected to the top of the fixed box 3. The cooler 8 cools the condensing plate 81. When natural gas passes through, the water inside the natural gas can be condensed on the surface of the condensing plate 81, thereby reducing the water content inside the natural gas and improving the treatment effect of natural gas.

[0028] Reference Figure 6 , Figure 7 and Figure 8In a preferred embodiment, a first connecting pipe 61 is fixedly connected to the center of the bottom of the lower connecting box 12. A first suction pump 6 is provided at one end of the first connecting pipe 61. The first suction pump 6 is located at the bottom of the deacidification tower 1. A second connecting pipe 62 is provided on the surface of the first suction pump 6. The top end of the second connecting pipe 62 is located on the surface of the fixed box 3. The connection between the second connecting pipe 62 and the fixed box 3 is located at the top of multiple heat sinks 82. Fixed plates 13 are horizontally fixedly connected to both sides of the surface of the deacidification tower 1. Support frames 14 are fixedly connected to the surfaces of both fixed plates 13. A first fixing member 15 is fixedly connected to the surface of one of the fixed plates 13. The second connecting pipe 62 is sleeved inside the first fixing member 15. A cooling box 4 is provided on the side of the surface of the deacidification tower 1 away from the first suction pump 6. A collecting pipe 41 is fixedly connected to the surface of the cooling box 4. The collecting pipe 41 is connected to the interior of the cooling box 4. The top end of the collecting pipe 41 is fixedly connected to the center of the bottom of the fixed box 3. A second suction pump 9 is provided on the side of the surface of the deacidification tower 1 away from the first suction pump 6. A second suction pump 9 is located between the deacidification tower 1 and the cooling box 4. A third connecting pipe 91 and a fourth connecting pipe 95 are mounted on the surface of the second suction pump 9. One end of the fourth connecting pipe 95 is fixedly connected to the surface of the cooling box 4 and communicates with the interior of the cooling box 4. Two spray pipes 93 are installed inside the deacidification tower 1. Both spray pipes 93 are horizontally arranged and located at the top of two horizontal pipes 7. Multiple spray heads 94 are installed at the bottom of each spray pipe 93. One end of each spray pipe 93... Two spray pipes 93 are fixedly connected to the same connecting branch pipe 92 at one end, and the top end of the third connecting pipe 91 is fixedly connected to the surface of the connecting branch pipe 92. The third connecting pipe 91 is used to circulate the solvent at the bottom of the deacidification tower 1 and transport the solvent to the inside of the fixed box 3. The solvent passes between the multiple heat sinks 82 on the cooler 8, thereby cooling the heat generated by the cooler 8 when it is working. At the same time, the solvent is heated, making it easier for the acidic gas inside to evaporate.

[0029] In this invention, the coordinated arrangement of two horizontal pipes 7 and multiple stirring pipes 71 facilitates thorough mixing of the natural gas supplied to the deacidification tower 1 with the internal solution, thereby promoting deacidification of the natural gas. Simultaneously, the solvent inside the deacidification tower 1 is circulated and heated, releasing acidic gases and allowing for solvent recycling. This also cools the surface of the cooler 8, further dehydrating the deacidified natural gas and improving the overall efficiency of the device. The deacidification tower 1 contains a solvent capable of absorbing acidic gases. During use, the gas requiring deacidification can be connected to one end of the feed pipe 5 via a pipeline, and then the valves 52 on the surfaces of the two feed branch pipes 51 can be opened. The gas to be deacidified is then fed into the two horizontal pipes 7 through two feed branch pipes 51 and two valves 52. The geared motor 74 is then driven, and the two horizontal pipes 7 rotate simultaneously under the connection of two gears 73. With the action of multiple stirring pipes 71, the natural gas to be deacidified is mixed with the solvent inside the deacidification tower 1. The rotation of the two horizontal pipes 7 and the multiple stirring pipes 71 further ensures thorough mixing of the natural gas and solvent. The natural gas is then conveyed upwards, where it is blocked by a conical baffle 21, which also reduces the moisture content within the natural gas. The gas then passes through the conical baffle... The baffle 21 is conveyed upwards, and the worm gear 75 drives the worm wheel 101 to rotate. Through the connection of the rotating shaft 100 and the two connecting rods 103, the two scrapers 102 scrape away the water at the bottom of the conical baffle 21, and at the same time drive the cooler 8 to work. Then, through the action of the condensing plate 81, the water inside the natural gas is condensed, thereby greatly reducing the water vapor inside the natural gas. The processed natural gas can then be transported through the discharge pipe 23 at the top of the separator 2. During use, the first suction pump 6 and the second suction pump 9 are driven. The drive of the first suction pump 6 causes the solvent at the bottom of the deacidification tower 1 to be transported to the fixed box 3 through the first connecting pipe 61 and the second connecting pipe 62. Inside, the solvent generator is heated by multiple heat sinks 82, which releases acidic gases from the solvent and cools the heat sinks 82. The separated acidic gases are then transported through the exhaust pipe 31, while the heated solvent is transported to the cooling box 4 through the collection pipe 41. The cooling box 4 is a conventional technology that cools the solvent. The second suction pump 9 transports the solvent inside the cooling box 4 to the two connecting branch pipes 92 through the connection of the third connecting pipe 91 and the connecting branch pipe 92, and sprays it out through multiple spray nozzles 94, thus circulating the solvent and improving the efficiency of the device.

[0030] For ease of description, spatial relative terms such as "above," "on top of," "on the upper surface of," "above," etc., are used herein to describe the spatial positional relationship of a device or feature as shown in the figures to other devices or features. It should be understood that spatial relative terms are intended to encompass different orientations in use or operation beyond the orientation of the device as described in the figures. For example, if the device in the figures were inverted, a device described as "above" or "on top of" other devices or structures would subsequently be positioned as "below" or "under" other devices or structures. Thus, the exemplary term "above" can include both "above" and "below." The device may also be positioned in other different ways (rotated 90 degrees or in other orientations), and the spatial relative descriptions used herein will be interpreted accordingly.

[0031] It should be noted that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to limit the exemplary embodiments according to this application. As used herein, the singular form is intended to include the plural form as well, unless the context clearly indicates otherwise. Furthermore, it should be understood that when the terms "comprising" and / or "including" are used in this specification, they indicate the presence of features, steps, operations, devices, components, and / or combinations thereof.

[0032] It should be noted that the terms "first," "second," etc., in the specification, claims, and accompanying drawings of this application are used to distinguish similar objects and are not necessarily used to describe a specific order or sequence. It should be understood that such data can be interchanged where appropriate so that the embodiments of this application described herein can be implemented, for example, in orders other than those illustrated or described herein. Furthermore, the terms "comprising" and "having," and any variations thereof, are intended to cover non-exclusive inclusion; for example, a process, method, system, product, or apparatus that comprises a series of steps or units is not necessarily limited to those steps or units explicitly listed, but may include other steps or units not explicitly listed or inherent to such processes, methods, products, or apparatus.

[0033] The above description is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Any equivalent substitutions or modifications made by those skilled in the art within the scope of the technology disclosed in the present invention, based on the technical solution and inventive concept of the present invention, should be covered within the scope of protection of the present invention.

Claims

1. A natural gas deacidification device, comprising a deacidification tower (1) and a separation cylinder (2), characterized in that: The upper and lower ends of the deacidification tower (1) are respectively fixedly connected to an upper connection box (11) and a lower connection box (12); two transverse tubes (7) are rotatably connected inside the deacidification tower (1); the two transverse tubes (7) are both arranged horizontally; a plurality of stirring tubes (71) are fixedly connected to the surfaces of the two transverse tubes (7); a plurality of air outlet holes (72) are arranged on the surfaces of the plurality of stirring tubes (71); and a rotating mechanism for rotating the two transverse tubes (7) is provided on the surface of the deacidification tower (1); The separation cylinder (2) is fixedly connected to the top of the upper connection box (11), the separation cylinder (2) is connected to the inside of the deacidification tower (1), a discharge pipe (23) is fixedly connected to the center of the top of the separation cylinder (2), the discharge pipe (23) is connected to the inside of the separation cylinder (2), a conical baffle (21) is provided at the center of the bottom of the separation cylinder (2), a plurality of support rods (22) are fixedly connected to the surface of the conical baffle (21), the plurality of support rods (22) are evenly distributed in a ring shape, one end of the plurality of support rods (22) is fixedly connected to the inner wall of the separation cylinder (2), a wiper mechanism for the conical baffle (21) is provided inside the deacidification tower (1), and a water vapor separation mechanism is provided inside the separation cylinder (2); The rotating mechanism comprises a gear (73), one end of each of the two transverse tubes (7) is fixedly connected to a connecting shaft, the two connecting shafts are sleeved inside one end of the deacidification tower (1), two gears (73) are provided, the two gears (73) are respectively fixedly connected to one end of the two connecting shafts, the two gears (73) are meshed with each other, a side plate (16) is fixedly connected to one end of the surface of the deacidification tower (1) near the two gears (73), the side plate (16) is arranged on the surfaces of the two gears (73), a reduction motor (74) is installed on the surface of the side plate (16), and the output shaft of the reduction motor (74) is fixedly connected to the center of the surface of one of the gears (73); Two rotary joints (53) are installed on one end of the surface of the deacidification tower (1) away from the two gears (73), and the other ends of the two transverse tubes (7) are respectively installed on one end of the two rotary joints (53). A feed pipe (5) is provided on the end of the deacidification tower (1) away from the two gears (73). The feed pipe (5) is arranged horizontally, and one end of the feed pipe (5) is fixedly connected to two feed branch pipes (51). One end of the two feed branch pipes (51) is respectively installed on the other end of the two rotary joints (53), and valves (52) are installed on the surfaces of the two feed branch pipes (51); The wiper mechanism comprises a scraper (102); a rotating shaft (100) is vertically rotatably connected inside the deacidification tower (1); a first horizontal plate (17) and a second horizontal plate (18) are arranged inside the deacidification tower (1); the first horizontal plate (17) and the second horizontal plate (18) are both arranged horizontally; the bottom end of the rotating shaft (100) is rotatably connected to the top of the first horizontal plate (17); the rotating shaft (100) is sleeved inside the second horizontal plate (18); and the top end of the rotating shaft (100) is rotatably connected to the bottom center of the conical baffle (21); A worm wheel (101) is sleeved on the surface of the rotating shaft (100), a worm (75) is sleeved on the surface of one of the transverse tubes (7), the worm wheel (101) and the worm (75) cooperate with each other, two scrapers (102) are provided, both of the two scrapers (102) are rotatably connected to the bottom of the conical baffle (21), and connecting rods (103) are fixedly connected to the surface of the rotating shaft (100). Both of the connecting rods (103) are fixedly connected to the surface of the rotating shaft (100).

2. A natural gas deacidification device according to claim 1, characterized in that: The water vapor separation mechanism comprises a refrigerator (8), a fixing box (3) is fixedly connected to the arc surface of the separation cylinder (2), the fixing box (3) is communicated with the interior of the separation cylinder (2), the refrigerator (8) is installed inside the fixing box (3), a condensation plate (81) is fixedly connected to the interior of the separation cylinder (2), the condensation plate (81) is arranged in a circular shape, the condensation plate (81) and the inner wall of the separation cylinder (2) are mutually fitted, the condensation plate (81) is installed on the surface of the refrigerator (8), a plurality of heat sinks (82) are arranged inside the fixing box (3), the plurality of heat sinks (82) are arranged vertically, and the plurality of heat sinks (82) are installed on the surface of the refrigerator (8), the upper and lower ends of the fixing box (3) are arranged in a conical shape, and the top of the fixing box (3) is fixedly connected to an exhaust pipe (31).

3. A natural gas deacidification device according to claim 1, characterized in that: A first connecting pipe (61) is fixedly connected to the center of the bottom of the lower connecting box (12); a first suction pump (6) is arranged at one end of the first connecting pipe (61); the first suction pump (6) is arranged at the bottom of the deacidification tower (1); a second connecting pipe (62) is arranged on the surface of the first suction pump (6); the top end of the second connecting pipe (62) is arranged on the surface of the fixing box (3); the connection between the second connecting pipe (62) and the fixing box (3) is arranged on the top of a plurality of heat sinks (82); fixing plates (13) are horizontally fixedly connected to the symmetrical sides of the surface of the deacidification tower (1); the surfaces of the two fixing plates (13) are fixedly connected to support frames (14); the surface of one of the fixing plates (13) is fixedly connected to a first fixing member (15); and the second connecting pipe (62) is sleeved inside the first fixing member (15).

4. A natural gas deacidification device according to claim 3, characterized in that: A cooling box (4) is provided on the surface of the deacidification tower (1) on a side away from the first suction pump (6); a collecting pipe (41) is fixedly connected to the surface of the cooling box (4); the collecting pipe (41) is connected to the interior of the cooling box (4); and the top end of the collecting pipe (41) is fixedly connected to the bottom center of the fixing box (3).

5. A natural gas deacidification device according to claim 4, characterized in that: A second suction pump (9) is arranged at one end of the surface of the deacidification tower (1) away from the first suction pump (6); the second suction pump (9) is arranged between the deacidification tower (1) and the cooling box (4); a third connecting pipe (91) and a fourth connecting pipe (95) are installed on the surface of the second suction pump (9); one end of the fourth connecting pipe (95) is fixedly connected to the surface of the cooling box (4); and the fourth connecting pipe (95) is communicated with the interior of the cooling box (4).

6. A natural gas deacidification device according to claim 5, characterized in that: Two spray pipes (93) are arranged inside the deacidification tower (1). The two spray pipes (93) are arranged horizontally. The two spray pipes (93) are arranged at the tops of the two horizontal pipes (7). A plurality of spray heads (94) are arranged at the bottoms of the two spray pipes (93). One end of the two spray pipes (93) is inserted into one side of the surface of the deacidification tower (1). One end of the two spray pipes (93) is fixedly connected to the same connecting branch pipe (92). The top end of the third connecting pipe (91) is fixedly connected to the surface of the connecting branch pipe (92).

Images