Efficient desulfurization device for fuel gas

By introducing a multi-layer structure and component design into the fuel gas desulfurization device, and utilizing multiple processes of components such as triangular elastic plates, arc strips, and rotating plates, the problem of single-layer baffle demisters being unable to remove fine droplets has been solved, achieving a highly efficient flue gas demisting effect.

CN120900318APending Publication Date: 2025-11-07SUZHOU LOTTE CHEM TECH
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Patent Information

Application Number
CN202510969068.9
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2025-07-15
Publication Date
2025-11-07

AI Technical Summary

Technical Problem

In existing fuel gas desulfurization devices, single-layer baffle demisters are unable to completely remove fine droplets from flue gas, resulting in poor demisting performance.

Method used

The demisting shell adopts a multi-layer structure, including components such as triangular elastic plates, arc-shaped strips, concave strips, rotating plates, and scraping strips. By processing the mist in the flue gas multiple times, combined with the design of U-shaped tubes and inclined tubes, it achieves multiple adsorption and scraping, thereby improving the demisting effect.

Benefits of technology

Through multiple treatments, the efficiency of removing mist from flue gas was significantly improved, ensuring that the flue gas after demisting is almost free of liquid droplets, thus enhancing the overall demisting effect.

✦ Generated by Eureka AI based on patent content.

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Abstract

The invention discloses an efficient desulfurization device for fuel gas, belongs to the technical field of fuel gas, and aims to solve the problems that mist in smoke is difficult to completely remove, smoke after demisting still contains mist, and the demisting effect is reduced. The efficient desulfurization device comprises a demisting shell, and a plurality of triangular elastic pieces distributed circumferentially are fixed to one side of the inner side wall of the demisting shell; a first arc-shaped strip, a second arc-shaped strip, a third arc-shaped strip, a fourth arc-shaped strip and a fifth arc-shaped strip are fixed on one side of the inner side wall of the demisting shell; according to the device, mist in flue gas can be subjected to secondary treatment, and the mist in the rest of the flue gas subjected to secondary treatment can be finally treated through the arranged rotating plate, separation strips, scraping strips and contact columns, so that the mist in the flue gas can be completely removed through three-time mist treatment, and the demisting effect is improved.
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Description

TECHNICAL FIELD

[0001] The application belongs to the technical field of fuel gas, and particularly relates to a high-efficiency fuel gas desulfurization device. BACKGROUND

[0002] The existing fuel gas desulfurization device constitutes a complete system for treating sulfur-containing fuel gas. After the fuel gas is purified by desulfurization, liquid droplets are usually entrained in the flue gas to form mist. In order to remove the liquid droplets in the flue gas, a demister is usually arranged in the flue gas passage. The commonly used demister structure is relatively simple, mainly relying on a single layer of baffle. The baffle changes the flow direction of the flue gas, and uses the inertial effect to make the liquid droplets impact the wall and be removed.

[0003] However, this single-layer baffle demisting method has obvious defects: the demisting efficiency is limited, and it is difficult to completely capture and remove the fine liquid droplets in the flue gas. Therefore, a certain amount of liquid droplets (mist) still remains in the flue gas after the demister treatment, which reduces the overall demisting effect.

[0004] Therefore, there is a need for a high-efficiency fuel gas desulfurization device to solve the problem that it is difficult to completely remove the mist in the flue gas in the prior art, resulting in that the flue gas after demisting still contains mist, which reduces the demisting effect. SUMMARY

[0005] The purpose of the present application is to provide a high-efficiency fuel gas desulfurization device to solve the problems raised in the background.

[0006] To achieve the above purpose, the present application provides the following technical scheme: a high-efficiency fuel gas desulfurization device, comprising a demisting shell, a plurality of circumferentially distributed triangular elastic sheets are fixed on one side of the inner side wall of the demisting shell, a first arc-shaped strip, a second arc-shaped strip, a third arc-shaped strip, a fourth arc-shaped strip and a fifth arc-shaped strip are fixed on one side of the inner side wall of the demisting shell, a first concave strip, a second concave strip, a third concave strip and a fourth concave strip are fixed on one side of the inner side wall of the demisting shell, an outer shell is fixed on the other side of the inner side wall of the demisting shell, a rotating rod is movably connected to the middle of one side of the inner side wall of the outer shell, the outer side wall of the rotating rod is fixed with a rotating plate, a plurality of circumferentially distributed scraping strips are fixed on one side of the rotating plate, a plurality of circumferentially distributed separation strips are fixed on one side of the rotating plate, and a plurality of circumferentially distributed contact columns are fixed on one side of the rotating plate.

[0007] Further, the triangular elastic sheet is connected with a U-shaped tube through the side face close to the first arc-shaped strip, and one end of the U-shaped tube corresponds to the triangular position of the corresponding triangular elastic sheet.

[0008] Further, the housing inner side wall one side is provided with a first arc-shaped groove and a second arc-shaped groove, the first arc-shaped groove and the second arc-shaped groove are respectively located on both sides of the triangular elastic sheet, the housing lower portion is provided with a storage box, the first arc-shaped groove and the second arc-shaped groove inner side wall bottom are respectively connected with a first communication pipe, and the first communication pipe bottom end is in through connection with the storage box top surface.

[0009] Further, the first groove and the second groove form a first gap, the second groove and the third groove form a second gap, the third groove and the fourth groove form a third gap, and the three-channel pipe is fixed in the middle of the demisting shell inner side wall.

[0010] Further, the three-channel pipe is connected with two inclined pipes near the bottom of one side of the rotating rod, and one end of the inclined pipe is in through connection with one side of the housing.

[0011] Further, the demisting shell outer side wall bottom is provided with a short arc-shaped groove, the short arc-shaped groove inner side wall bottom is connected with a second communication pipe, and the second communication pipe bottom end is in through connection with the storage box top surface.

[0012] Further, the housing outer side wall bottom is connected with a third communication pipe, the third communication pipe bottom end is in through connection with the storage box top surface, and the third communication pipe outer side wall is connected with an exhaust pipe.

[0013] Further, the demisting shell inner side wall is fixed with a fixed plate on the other side, the fixed plate is fixed with a motor near one side of the housing, and the motor output end is fixed with one end of the rotating rod.

[0014] Further, the demisting shell one side is provided with a four-in-one combined heat exchanger, the demisting shell one end is connected with an L-shaped pipe, one end of the L-shaped pipe is in communication with the bottom of the four-in-one combined heat exchanger, one side of the four-in-one combined heat exchanger is provided with an air blower, one side of the air blower is provided with a heating furnace, the heating furnace bottom is provided with a burner, the other side of the demisting shell is provided with a flue gas corrosion prevention fan, one side of the flue gas corrosion prevention fan is provided with a chimney, the chimney outer side wall top is connected with an air inlet pipe, the burner bottom is connected with a fuel gas system pipeline, one end of the fuel gas system pipeline is in communication with the top of the four-in-one combined heat exchanger outer side wall, the burner outer side wall, the air blower output end and the four-in-one combined heat exchanger outer side wall top are connected with an air system pipeline, the heating furnace, the four-in-one combined heat exchanger and the chimney are connected with a flue gas system pipeline, one end of the exhaust pipe is in communication with the air inlet end of the flue gas corrosion prevention fan, and the air outlet end of the flue gas corrosion prevention fan is in communication with the chimney.

[0015] Compared with the prior art, the fuel gas efficient desulfurization device provided by the application has at least the following beneficial effects: The mist in the flue gas can be adsorbed on the triangular elastic sheet, the triangular elastic sheet can swing through the cooperation of the U-shaped tube and the triangular elastic sheet, and the liquid drops on the triangular elastic sheet are shaken off, so that the mist in the flue gas is preliminarily treated; the mist in the flue gas can be secondarily treated through the first arc-shaped strip, the second arc-shaped strip, the third arc-shaped strip, the fourth arc-shaped strip, the fifth arc-shaped strip, and the first concave strip, the second concave strip, the third concave strip and the fourth concave strip; the mist in the remaining part of the flue gas after two treatments can be finally treated through the rotating plate, the separation strip, the scraping strip and the contact column, so that the mist in the flue gas can be completely removed through three mist treatments, and the demisting effect is improved. BRIEF DESCRIPTION OF DRAWINGS

[0016] Figure 1 It is a schematic diagram of the overall structure of the application; Figure 2 It is a schematic diagram of the three-channel pipe structure of the application; Figure 3 It is a schematic diagram of the side view structure of the third arc-shaped strip of the application; Figure 4 It is a schematic diagram of the U-shaped tube structure of the application; Figure 5 It is a schematic diagram of the shell structure of the application.

[0017] In the drawings: 100, heating furnace; 101, burner; 102, air system pipeline; 103, air blower; 104, four-in-one combined heat exchanger; 105, demisting shell; 106, flue gas corrosion prevention fan; 107, chimney; 108, fuel gas system pipeline; 109, flue gas system pipeline; 110, air inlet pipe; 200, triangular elastic sheet; 201, U-shaped tube; 202, first arc-shaped groove; 203, second arc-shaped groove; 204, first communication pipe; 205, storage tank; 300, first arc-shaped strip; 301, second arc-shaped strip; 302, third arc-shaped strip; 303, fourth arc-shaped strip; 304, fifth arc-shaped strip; 305, short arc-shaped groove; 306, second communication pipe; 400, first concave strip; 401, second concave strip; 402, third concave strip; 403, fourth concave strip; 500, three-channel pipe; 501, inclined pipe; 600, shell; 601, rotating rod; 602, scraping strip; 603, separation strip; 604, contact column; 605, third communication pipe; 606, exhaust pipe; 607, rotating plate; 700, fixing plate; 701, motor. DETAILED DESCRIPTION

[0018] To make the objectives, technical solutions and advantages of the embodiments of the present application clearer, the technical solutions in the embodiments of the present application will be described clearly and completely below with reference to the drawings in the embodiments of the present application. Obviously, the described embodiments are only some but not all of the embodiments of the present application. It should be explained that, in the case of no conflict, the embodiments and the features in the embodiments in the present disclosure can be combined, separated, interchanged and / or rearranged. Based on the embodiments in the present application, all other embodiments obtained by those skilled in the art without creative work are within the scope of protection of the present application.

[0019] In the drawings, the size and relative sizes of parts can be exaggerated for clarity and / or descriptive purposes. When the exemplary embodiments can be carried out in different sequences, a specific process sequence can be performed in a different order from the described order. For example, two consecutively described processes can be performed substantially simultaneously or in an order opposite to the described order. In addition, the same reference numerals represent the same parts.

[0020] The terms used herein are for the purpose of describing specific embodiments and are not intended to be limiting. As used herein, the singular forms "a," "an," and "the" are intended to include the plural forms as well, unless the context clearly indicates otherwise. Furthermore, to the extent that the terms "including" and / or "containing" and variations thereof are used in either the detailed description or the claims, such terms are intended to be inclusive in a manner similar to the term "comprising" and / or "including" and / or "containing" as an open-ended transition. It is also noted that, as used herein, the terms "substantially," "approximately," and other similar terms are used as synonyms for "about," and are employed to account for inherent variations in measuring, calculating, and / or providing a value or quantity.

[0021] Reference will now be made to Figures 1-5The application provides a fuel gas efficient desulfurization device, which comprises a demisting shell 105, a plurality of circumferentially distributed triangular elastic sheets 200 are fixed on one side of the inner side wall of the demisting shell 105, a first arc-shaped strip 300, a second arc-shaped strip 301, a third arc-shaped strip 302, a fourth arc-shaped strip 303 and a fifth arc-shaped strip 304 are fixed on one side of the inner side wall of the demisting shell 105, a first concave strip 400, a second concave strip 401, a third concave strip 402 and a fourth concave strip 403 are fixed on one side of the inner side wall of the demisting shell 105, an outer shell 600 is fixed on the other side of the inner side wall of the demisting shell 105, a rotating rod 601 is movably connected to the middle of one side of the inner side wall of the outer shell 600, a rotating plate 607 is fixed on the outer side wall of the rotating rod 601, a plurality of circumferentially distributed scraping strips 602 are fixed on one side of the rotating plate 607, a plurality of circumferentially distributed separation strips 603 are fixed on one side of the rotating plate 607, and a plurality of circumferentially distributed contact columns 604 are fixed on one side of the rotating plate 607.

[0022] As a further scheme of the application, the U-shaped pipe 201 is through-connected on one side of the triangular elastic sheet 200 close to the first arc-shaped strip 300, and one end of the U-shaped pipe 201 corresponds to the triangular position of the corresponding triangular elastic sheet 200.

[0023] The U-shaped pipe 201 is arranged, so that part of flue gas entering through the L-shaped pipe can enter from the U-shaped pipe 201, and then is discharged from the other end of the U-shaped pipe 201 and impacts the triangular elastic sheet 200, so that the triangular elastic sheet 200 swings. The other end of the U-shaped pipe 201 is a certain distance away from the triangular elastic sheet 200, so that the triangular elastic sheet 200 does not contact the other end of the U-shaped pipe 201 when swinging, avoiding that the other end of the U-shaped pipe 201 contacts the triangular elastic sheet 200 and blocks the triangular elastic sheet 200.

[0024] As a further scheme of the application, the first arc-shaped groove 202 and the second arc-shaped groove 203 are arranged on one side of the inner side wall of the outer shell 600, the first arc-shaped groove 202 and the second arc-shaped groove 203 are respectively located on the two sides of the triangular elastic sheet 200, a storage box 205 is arranged below the outer shell 600, the first communication pipe 204 is through-connected to the bottom of the inner side wall of the first arc-shaped groove 202 and the second arc-shaped groove 203, and the bottom end of the first communication pipe 204 is through-connected to the top surface of the storage box 205.

[0025] By setting the first arc-shaped groove 202 and the second arc-shaped groove 203, when the triangular elastic sheet 200 swings to adsorb the liquid drops in the flue gas, the liquid drops adsorbed on the triangular elastic sheet 200 can be swung into the first arc-shaped groove 202 and the second arc-shaped groove 203 along with the swing of the triangular elastic sheet 200, and then enter the first communication pipe 204, and finally enter the storage tank 205 to realize the storage of the liquid drops, and when the triangular elastic sheet 200 swings, the flue gas can pass through the gap between adjacent triangular elastic sheets 200, so that the liquid drops in the flue gas can be preliminarily treated.

[0026] As a further scheme of the present application, the first gap is formed between the first groove 400 and the second groove 401, the second gap is formed between the second groove 401 and the third groove 402, the third gap is formed between the third groove 402 and the fourth groove 403, and the three-channel pipe 500 is fixed in the middle of the inner side wall of the demisting shell 105, the three-channel pipe 500 has three ports, and the three ports of the three-channel pipe 500 correspond to the first gap, the second gap and the third gap respectively.

[0027] Through the setting of the three-channel pipe 500, the flue gas discharged from the first gap, the second gap and the third gap can enter the three-channel pipe 500 from the three ports of the three-channel pipe 500, and then enter the inclined pipe 501, so that the flue gas after secondary treatment can be collected, and then the flue gas after secondary treatment can enter the tertiary treatment process.

[0028] The first port of the three-channel pipe 500 is fixed to the bottom and the top of the first groove 400 and the second groove 401 respectively, the second port of the three-channel pipe 500 is fixed to the bottom and the top of the second groove 401 and the third groove 402 respectively, the third port of the three-channel pipe 500 is fixed to the bottom and the top of the third groove 402 and the fourth groove 403 respectively, the top of the first groove 400 is fixed to the inner wall of the first arc-shaped strip 300, the top of the first arc-shaped strip 300 is fixed to the top of the inner side wall of the demisting shell 105, and the bottom of the fourth groove 403 is fixed to the bottom of the inner side wall of the demisting shell 105. As a further scheme of the present application, two inclined pipes 501 are connected to the bottom of the side of the three-channel pipe 500 close to the rotating rod 601, and one end of the inclined pipe 501 is connected to the side surface of the shell 600.

[0029] Through the setting of the inclined pipe 501, the flue gas after secondary treatment can enter the shell 600 through the inclined pipe 501 for tertiary treatment.

[0030] As a further scheme of the present application, a short arc-shaped groove 305 is arranged at the bottom of one side of the outer wall of the demisting shell 105, a second communicating pipe 306 is connected through the bottom of the inner wall of the short arc-shaped groove 305, and the bottom end of the second communicating pipe 306 is connected through the top surface of the storage tank 205.

[0031] The short arc-shaped groove 305 is arranged to enable the liquid drops falling from the outer wall of the fifth arc-shaped strip 304 to enter the short arc-shaped groove 305 for collection, then enter the second communicating pipe 306, and finally enter the storage tank 205, so that the liquid drops collected after secondary treatment can be collected.

[0032] As a further scheme of the present application, a third communicating pipe 605 is connected through the bottom of the outer wall of the shell 600, the bottom end of the third communicating pipe 605 is connected through the top surface of the storage tank 205, and an exhaust pipe 606 is connected through the outer wall of the third communicating pipe 605.

[0033] The third communicating pipe 605 is arranged to enable the liquid drops collected after third treatment in the shell 600 to enter the storage tank 205 through the third communicating pipe 605, and enable the flue gas after third treatment to enter the exhaust pipe 606 through the third communicating pipe 605, then enter the flue gas corrosion prevention fan 106, and the inclination of the exhaust pipe 606 avoids the liquid drops entering the third communicating pipe 605 from entering the exhaust pipe 606.

[0034] As a further scheme of the present application, a fixed plate 700 is fixed to the other side of the inner wall of the demisting shell 105, a motor 701 is fixed to one side of the fixed plate 700 close to the shell 600, and one end of the motor 701 is fixed to one end of the rotating rod 601.

[0035] The fixed plate 700 is arranged to enable the motor 701 to be fixed, and the motor 701 is arranged to enable the rotating rod 601 to rotate.

[0036] As a further scheme of the present application, the demisting shell 105 is provided with a four-in-one combined heat exchanger 104 on one side, one end of the demisting shell 105 is connected with an L-shaped pipe, one end of the L-shaped pipe is communicated with the bottom of the four-in-one combined heat exchanger 104, the four-in-one combined heat exchanger 104 is provided with an air blower 103 on one side, the air blower 103 is provided with a heating furnace 100 on one side, the heating furnace 100 is provided with a burner 101 at the bottom, the other side of the demisting shell 105 is provided with a flue gas corrosion prevention blower 106, the flue gas corrosion prevention blower 106 is provided with a chimney 107 on one side, the top of the outer side wall of the chimney 107 is communicated with an air inlet pipe 110, the bottom of the burner 101 is communicated with a fuel gas system pipe 108, one end of the fuel gas system pipe 108 is communicated with the top of the outer side wall of the four-in-one combined heat exchanger 104, an air system pipe 102 is connected between the outer side wall of the burner 101, the output end of the air blower 103 and the top of the outer side wall of the four-in-one combined heat exchanger 104, a flue gas system pipe 109 is connected between the heating furnace 100, the four-in-one combined heat exchanger 104 and the chimney 107, one end of the exhaust pipe 606 is communicated with the air inlet end of the flue gas corrosion prevention blower 106, and the air outlet end of the flue gas corrosion prevention blower 106 is communicated with the chimney 107.

[0037] The four-in-one combined heat exchanger 104 comprises an air preheater section, a fuel heating section, a flue gas condensation corrosion prevention section and a condensed water neutralization treatment device.

[0038] In summary: The hot flue gas from the convection chamber of the heating furnace 100 is exchanged with cold air and fuel gas through the four-in-one combined heat exchanger 104 to reduce the temperature to 80℃, and the low-temperature flue gas passes through the demisting shell 105 to remove the uncondensed mist in the cold flue gas, and the demisted cold flue gas is sent into the chimney 107 by the flue gas corrosion prevention blower 106 and discharged into the atmosphere. The hot flue gas enters the fuel gas system pipe 108 through the air inlet pipe 110, and then enters the heating furnace 100. The condensed water produced by the flue gas condensation corrosion prevention section is neutralized and discharged after passing through the condensed water neutralization treatment device (the condensed water is acidic, and after neutralization, it becomes weakly alkaline and can be directly discharged up to standard).

[0039] Air system process: The cold air from the air suction port (the air inlet end of the air blower 103) is sent into the four-in-one combined heat exchanger 104 through the air blower 103 after being exchanged with the flue gas, and then is sent into the heating furnace 100 through the air system pipe 102, and the burner 101 is used for combustion.

[0040] Fuel gas system process: The fuel gas (~40℃) from the device is heated by the fuel heating section of the four-in-one combined heat exchanger 104, and then is sent into the heating furnace 100 through the fuel gas system pipe 108 to be used for combustion by the burner 101.

[0041] When the flue gas is defogged, the servo motor 701 is started, the flue gas first enters the defogging shell 105 through the L-shaped pipe, then the flue gas impacts the triangular elastic sheet 200, so that the mist in the flue gas contacts the triangular elastic sheet 200 and gradually forms droplets, then the droplets on the triangular elastic sheet 200 are brought down by the swing of the triangular elastic sheet 200 and enter the first arc-shaped groove 202, and then enter the storage tank 205 through the first connecting pipe 204; the flue gas impacts the triangular elastic sheet 200, so that the triangular elastic sheet 200 deforms, part of the flue gas enters the U-shaped pipe 201, then is discharged from one end of the U-shaped pipe 201 and impacts the triangular elastic sheet 200, the mist in this part of the flue gas contacts the other side of the triangular elastic sheet 200 and gradually forms droplets, then is brought down by the swing of the triangular elastic sheet 200 and enters the second arc-shaped groove 203, and then enters the storage tank 205; the impact directions of the two parts of the flue gas are opposite, so that the elastic sheet swings, at this time, gaps are formed between the elastic sheets, a small part of the flue gas passes through the gaps and impacts the first arc-shaped bar 300, the second arc-shaped bar 301, the third arc-shaped bar 302, the fourth arc-shaped bar 303 and the fifth arc-shaped bar 304, the mist in the flue gas contacting the first arc-shaped bar 300, the second arc-shaped bar 301, the third arc-shaped bar 302, the fourth arc-shaped bar 303 and the fifth arc-shaped bar 304 adheres to the outer side wall of the first arc-shaped bar 300, the second arc-shaped bar 301, the third arc-shaped bar 302, the fourth arc-shaped bar 303 and the fifth arc-shaped bar 304, as the mist adheres more and more, droplets are formed and slide from the first arc-shaped bar 300, the second arc-shaped bar 301, the third arc-shaped bar 302, the fourth arc-shaped bar 303 and the fifth arc-shaped bar 304 in turn, and finally enter the short arc-shaped groove 305, and another part of the flue gas passes through the gaps between adjacent arc-shaped bars and impacts the first concave bar 400, the second concave bar 401, the third concave bar 402 and the fourth concave bar 403, and adheres to the inner wall of the first concave bar 400, the second concave bar 401, the third concave bar 402 and the fourth concave bar 403, finally forms droplets, when the weight of the droplets is greater than the adsorption force, the droplets slide from the first concave bar 400, the second concave bar 401, the third concave bar 402 and the fourth concave bar 403 in turn to the short arc-shaped groove 305, and then enter the second connecting pipe 306, and finally enter the storage tank 205 for storage;The part of the flue gas impacting the first groove 400, the second groove 401, the third groove 402 and the fourth groove 403 enters the three-channel pipe 500 through the gap between the adjacent grooves, and then enters the inclined pipe 501, and finally enters the shell 600. The servo motor 701 rotates to drive the rotating rod 601 to rotate, the rotating rod 601 drives the rotating plate 607 to rotate, and then drives the scraping strip 602, the partition strip 603 and the contact column 604 to rotate. The flue gas entering the shell 600 enters between the contact columns 604. With the rotation of the contact columns 604, the mist in the flue gas is gradually adsorbed on the contact columns 604, and is thrown to the inner wall of the shell 600 under the action of centrifugal force. The scraping strip 602 rotates to scrape the liquid drops on the inner wall of the shell 600 into the third communication pipe 605, and finally into the storage tank 205. The finally treated flue gas enters the third communication pipe 605 and is discharged into the flue gas corrosion prevention fan 106 through the exhaust pipe 606. After the treatment of the flue gas corrosion prevention fan 106, the flue gas enters the chimney 107, and is finally discharged into the external environment from the chimney 107.

[0042] The heating furnace 100, the burner 101, the air blower 103, the flue gas corrosion prevention fan 106 and the condensate water neutralization and treatment device can be purchased in the market, which are mature technologies in the field and have been fully disclosed, so the description is not repeated.

[0043] Although the embodiments of the present application have been shown and described, it can be understood by those skilled in the art that various changes, modifications, replacements and variations can be made to the embodiments without departing from the principles and spirits of the present application, and the scope of the present application is defined by the appended claims and their equivalents.

Claims

1. A fuel gas high-efficiency desulfurization device comprising a mist eliminator shell (105), characterized in that, The inside wall of the demisting shell (105) is fixed with a plurality of circumferentially distributed triangular elastic pieces (200), the inside wall of the demisting shell (105) is fixed with a first arc-shaped strip (300), a second arc-shaped strip (301), a third arc-shaped strip (302), a fourth arc-shaped strip (303) and a fifth arc-shaped strip (304), the inside wall of the demisting shell (105) is fixed with a first concave strip (400), a second concave strip (401), a third concave strip (402) and a fourth concave strip (403), the other side of the inside wall of the demisting shell (105) is fixed with a shell (600), the middle of the inner side wall of the shell (600) is movably connected with a rotating rod (601), the outer side wall of the rotating rod (601) is fixed with a rotating plate (607), the one side of the rotating plate (607) is fixed with a plurality of circumferentially distributed scraping strips (602), the one side of the rotating plate (607) is fixed with a plurality of circumferentially distributed separation strips (603), and the one side of the rotating plate (607) is fixed with a plurality of circumferentially distributed contact columns (604).

2. A fuel gas high efficiency desulfurization device according to claim 1, characterized in that: The U-shaped pipe (201) is connected through the one side of the triangular elastic piece (200) close to the first arc-shaped strip (300), and one end of the U-shaped pipe (201) corresponds to the triangular position of the corresponding triangular elastic piece (200).

3. The device for high-efficient desulfurization of fuel gas according to claim 1, characterized in that: The inside wall of the shell (600) is provided with a first arc-shaped groove (202) and a second arc-shaped groove (203) on one side, the first arc-shaped groove (202) and the second arc-shaped groove (203) are located on the two sides of the triangular elastic piece (200) respectively, a storage box (205) is arranged below the shell (600), the bottom of the inside wall of the first arc-shaped groove (202) and the second arc-shaped groove (203) is connected through a first communication pipe (204) respectively, and the bottom end of the first communication pipe (204) is connected through the top surface of the storage box (205).

4. The fuel gas high-efficiency desulfurization device according to claim 1, characterized in that: The first concave strip (400) and the second concave strip (401) form a first gap, the second concave strip (401) and the third concave strip (402) form a second gap, the third concave strip (402) and the fourth concave strip (403) form a third gap, and a three-channel pipe (500) is fixed in the middle of the inside wall of the demisting shell (105), the three-channel pipe (500) has three ports, and the three ports of the three-channel pipe (500) correspond to the first gap, the second gap and the third gap respectively.

5. The fuel gas high-efficiency desulfurization device according to claim 4, characterized in that: The three-channel pipe (500) is connected through two inclined pipes (501) at the bottom of the one side close to the rotating rod (601), and one end of the inclined pipe (501) is connected through the one side of the shell (600).

6. The fuel gas high-efficiency desulfurization device according to claim 1, characterized in that: The bottom of the one side of the outside wall of the demisting shell (105) is provided with a short arc-shaped groove (305), the bottom of the inside wall of the short arc-shaped groove (305) is connected through a second communication pipe (306), and the bottom end of the second communication pipe (306) is connected through the top surface of the storage box (205).

7. The fuel gas high-efficiency desulfurization device according to claim 1, characterized in that: The outer shell (600) outer side wall bottom through connection has the third communication pipe (605), the third communication pipe (605) bottom end with the storage tank (205) top surface through connection, the third communication pipe (605) outer side wall through connection has the exhaust pipe (606).

8. The fuel gas high-efficiency desulfurization device according to claim 1, characterized in that: The inner side wall of the demisting shell (105) is fixed with a fixed plate (700) on the other side, the fixed plate (700) is fixed with a motor (701) on the side close to the outer shell (600), and the output end of the motor (701) is fixed with the rotating rod (601).

9. The fuel gas high-efficiency desulfurization device according to claim 1, characterized in that: The demisting shell (105) is provided with a four-in-one combined heat exchanger (104) on one side, an L-shaped pipe is connected to one end of the demisting shell (105), one end of the L-shaped pipe is communicated with the bottom of the four-in-one combined heat exchanger (104), an air blower (103) is arranged on one side of the four-in-one combined heat exchanger (104), a heating furnace (100) is arranged on one side of the air blower (103), a burner (101) is arranged at the bottom of the heating furnace (100), a flue gas corrosion prevention fan (106) is arranged on the other side of the demisting shell (105), a chimney (107) is arranged on one side of the flue gas corrosion prevention fan (106), an air inlet pipe (110) is communicated with the top of the outer side wall of the chimney (107), a fuel gas system pipeline (108) is communicated with the bottom of the burner (101), one end of the fuel gas system pipeline (108) is communicated with the top of the outer side wall of the four-in-one combined heat exchanger (104), an air system pipeline (102) is connected between the outer side wall of the burner (101), the output end of the air blower (103) and the top of the outer side wall of the four-in-one combined heat exchanger (104), a flue gas system pipeline (109) is connected between the heating furnace (100), the four-in-one combined heat exchanger (104) and the chimney (107), one end of the exhaust pipe (606) is communicated with the air inlet end of the flue gas corrosion prevention fan (106), and the air outlet end of the flue gas corrosion prevention fan (106) is communicated with the chimney (107).