Monensin cyclone separator

Abstract

The application provides a monensin cyclone separation device, which comprises a water removal tank, an air inlet and an air outlet are arranged on the water removal tank, and a plurality of water absorption units are sequentially arranged in the water removal tank from top to bottom, a plurality of diffusion through holes are uniformly arranged on each water absorption unit; wherein the air inlet is arranged on the side wall of the water removal tank and is lower than the lowermost water absorption unit, a first pipeline is communicated with the air inlet, and the end of the first pipeline away from the water removal tank is used for connecting the exhaust port of a monensin production device; the air outlet is arranged on the top of the water removal tank and is communicated with a second pipeline; a cyclone separator body, the air inlet of the cyclone separator body is communicated with the end of the second pipeline away from the water removal tank, and the cyclone separator body is used for separating gas and solid to obtain monensin particles from the waste gas containing monensin particles after water removal by the water removal tank. The application reduces the adhesion of monensin to the inner wall of the cyclone separator body as much as possible, thereby improving the separation effect of the cyclone separator body on monensin.

Description

Technical Field

[0001] This application relates to the field of cyclone separation technology, and in particular to a monensin cyclone separation device. Background Technology

[0002] Monensin, also known as "rumen extract," is a widely used feed additive for ruminants. Originally a substance secreted by Streptomyces, it controls the proportion of volatile fatty acids in the rumen, reduces protein degradation in the rumen, lowers feed dry matter consumption, improves nutrient utilization, and enhances animal energy utilization. Because monensin particles are carried in the waste gas generated during the flash drying process of monensin premixes or refined products, it is usually necessary to separate these particles from the waste gas to improve monensin yield.

[0003] However, existing methods typically use cyclone separators to separate monensin particles from the waste gas generated during the flash drying process of monensin premixes or refined products. Because the waste gas from this process contains a certain amount of moisture, monensin easily adheres to the conveying pipes and the walls of the cyclone separator during separation. This affects the transport of the waste gas and the normal operation of the cyclone separator, resulting in poor separation efficiency and a low monensin yield. Therefore, this application provides a monensin cyclone separation device. Utility Model Content

[0004] This application provides a monensin cyclone separator to solve the technical problems described in the background art.

[0005] To solve the above-mentioned technical problems, this application adopts the following technical solution: This application provides a monensin cyclone separator, comprising: The water removal tank is provided with an air inlet and an air outlet, and multiple water absorption units are arranged in sequence from top to bottom inside the tank. Each water absorption unit is provided with multiple diffusion holes evenly distributed. The air inlet is located on the side wall of the dewatering tank and is lower than the bottom water absorption unit. A first pipe is connected to the air inlet. The end of the first pipe away from the dewatering tank is used to connect to the exhaust port of the monensin production device. The air outlet is located at the top of the dewatering tank and is connected to a second pipe. The cyclone separator body has an air inlet connected to the end of the second pipe away from the dewatering tank, and is used to perform gas-solid separation on the waste gas containing monensin particles that has been dewatered by the dewatering tank to obtain monensin particles.

[0006] Optionally, a door is sealed on the side wall of the water removal tank; The water removal tank has multiple first mounting slots and multiple second mounting slots on its two opposite inner sidewalls. Each first mounting slot is directly opposite a second mounting slot, and the multiple first mounting slots and multiple second mounting slots correspond one-to-one with the multiple water absorption units.

[0007] Optionally, each of the water-absorbing units includes a housing, a top plate, and a plurality of water-absorbing balls; The opposite sides of the housing are respectively disposed in the first mounting groove and the second mounting groove. One side of the top plate is hinged to the top of the housing and is used to make the housing in an open or closed state. A plurality of diffusion holes are evenly opened on the bottom wall of the housing and the top plate. A plurality of water-absorbing balls are disposed in the housing and their diameter is larger than the diameter of the diffusion holes.

[0008] Optionally, the absorbent ball is made of silicone or calcium chloride.

[0009] Optionally, the diameter of the diffusion through hole is 1mm to 3mm.

[0010] Optionally, a vibrator is provided on the outer wall of the lower section of the cyclone separator body.

[0011] Optionally, the outlet of the cyclone separator body is connected to a waste gas treatment device through a third pipe. An induced draft fan is installed on the third pipeline.

[0012] Optionally, the discharge port of the cyclone separator body is connected to a monensin collection tank via a fourth pipe. The fourth pipeline is equipped with a discharge valve.

[0013] The monensin cyclone separator provided in this application uses a dewatering tank to allow monensin waste gas to enter through a first pipe. Within the dewatering tank, the gas gradually diffuses upwards before entering the cyclone separator body through a second pipe. During this upward diffusion, the monensin waste gas sequentially contacts multiple water-absorbing units arranged from bottom to top within the tank. These units absorb moisture from the monensin waste gas, reducing its moisture content and minimizing the adhesion of monensin particles to the inner wall of the cyclone separator due to high humidity. This ensures effective separation and improves the monensin yield. In addition, the multiple diffusion holes evenly opened on each water absorption unit can not only allow monensin waste gas to diffuse, but also disperse the monensin waste gas, so that the monensin waste gas can fully contact the water absorption unit, thereby improving the water removal efficiency of the water absorption unit for monensin waste gas. Attached Figure Description

[0014] To more clearly illustrate the technical solutions in the embodiments of this application or the prior art, the drawings used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the 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.

[0015] Figure 1 This is a schematic diagram of the structure of a monensin cyclone separator provided in an embodiment of this application; Figure 2 This is a schematic diagram of the structure of a water removal tank provided in one embodiment of this application; Figure 3 This is a schematic diagram of the internal structure of a water removal tank provided in an embodiment of this application; Figure 4 This is a schematic diagram of the structure of a water absorption unit provided in an embodiment of this application.

[0016] In the diagram: 100, water tank; 101, first pipe; 102, second pipe; 103, door; 104, first mounting slot; 105, second mounting slot; 200, water suction unit; 201, diffuser hole; 202, housing shell; 203, top plate; 204, water suction ball; 300, monensin production device; 400, cyclone separator body; 401, vibrator; 500, third pipe; 501, waste gas treatment device; 502, induced draft fan; 600, fourth pipe; 601, monensin collection tank; 602, unloading valve. Detailed Implementation

[0017] To make the objectives, technical solutions, and advantages of the embodiments of this application clearer, the technical solutions in the embodiments of this application are described clearly and completely below. Obviously, the described embodiments are only some embodiments of this application, not all embodiments. Based on the embodiments in this application, all other embodiments obtained by those skilled in the art without creative effort are also within the scope of protection of this application.

[0018] refer to Figures 1 to 4 This application provides a monensin cyclone separator, comprising: The dewatering tank 100 is equipped with an air inlet and an air outlet, and multiple water absorption units 200 are arranged sequentially from top to bottom inside the tank. Each water absorption unit 200 has multiple evenly distributed diffusion holes 201. These diffusion holes 201 allow monensin entering the dewatering tank 100 to diffuse, and also disperse the monensin exhaust gas entering the tank 100, ensuring a more even distribution and more thorough contact between the monensin exhaust gas and the water absorption units 200. Furthermore, the water absorption units 200 are detachable within the dewatering tank 100 for easy replacement, ensuring that the water absorption performance of each unit 200 maintains optimal capacity throughout.

[0019] The air inlet is located on the side wall of the dewatering tank 100 and is lower than the lowest water absorption unit 200. A first pipe 101 is connected to the air inlet. The end of the first pipe 101 away from the dewatering tank 100 is connected to the exhaust port of the monensin production device 300. The air outlet is located at the top of the dewatering tank 100 and is connected to a second pipe 102. Specifically, the monensin waste gas enters the dewatering tank 100 from the exhaust port of the monensin production device 300 through the first pipe 101 and diffuses from bottom to top inside the dewatering tank 100. During the diffusion process, the monensin waste gas comes into full contact with multiple water absorption units 200 from bottom to top inside the dewatering tank 100, so that the water absorption units 200 absorb as much moisture as possible from the monensin waste gas, thereby reducing the water content in the monensin waste gas.

[0020] The cyclone separator body 400 has its air inlet connected to the end of the second pipe 102 furthest from the dewatering tank 100. It is used to perform gas-solid separation on the waste gas containing monensin particles that has been dewatered by the dewatering tank 100 after entering the cyclone separator body 400, in order to obtain monensin particles. The structure and separation principle of the cyclone separator body 400 are readily available in existing cyclone separators and are not considered innovative points of this application; therefore, they will not be described in detail here.

[0021] The monensin cyclone separator provided in this application, by setting up a dewatering tank 100, allows monensin waste gas to enter the dewatering tank 100 through the first pipe 101. After gradually diffusing from bottom to top in the dewatering tank 100, it enters the cyclone separator body 400 through the second pipe 102. During the process of diffusing from bottom to top in the dewatering tank 100, the monensin waste gas sequentially contacts multiple water absorption units 200 from bottom to top in the dewatering tank 100. In this way, the multiple water absorption units 200 sequentially absorb the moisture in the monensin waste gas, thereby reducing the moisture content in the monensin waste gas entering the cyclone separator body 400. This minimizes the situation where monensin particles adhere to the inner wall of the cyclone separator body 400 due to high humidity, thus ensuring the separation effect of the cyclone separator body 400 and improving the yield of monensin. In addition, the multiple diffusion holes 201 evenly opened on each water absorption unit 200 can not only allow monensin waste gas to diffuse, but also disperse the monensin waste gas, so that the monensin waste gas can fully contact the water absorption unit 200, thereby improving the water removal efficiency of the water absorption unit 200 for monensin waste gas.

[0022] In some embodiments, reference Figure 2 and Figure 3 In this application, a door 103 is sealed on the side wall of the water removal tank 100. Since the water absorption performance of the water absorption unit 200 may decrease after a period of use, opening the door 103 makes it convenient to replace the water absorption unit 200 inside the water removal tank 100.

[0023] In addition, multiple first mounting slots 104 and multiple second mounting slots 105 are respectively provided on the two opposite inner side walls of the water tank 100. Each first mounting slot 104 is directly opposite a second mounting slot 105, and the multiple first mounting slots 104 and multiple second mounting slots 105 correspond one-to-one with multiple water suction units 200. The side wall of the water tank 100 with the door 103 is perpendicular to the side wall with the first mounting slots 104 and the second mounting slots 105. For example, if the door 103 is located on the front side wall of the water tank 100, then the first mounting slots 104 and the second mounting slots 105 are located on the left inner side wall and the right inner side wall, or the right inner side wall and the inner left side wall, respectively.

[0024] In the above embodiments, after the water absorption unit 200 has been used for a period of time (the specific time can be set according to the water absorption performance of the water absorption unit 200 and the usage time, for example, it can be 10 days or other days, but this application does not further limit it here), the water absorption unit 200 is pulled out from the first mounting groove 104 and the second mounting groove 105, and the pre-prepared water absorption unit 200 is placed into the first mounting groove 104 and the second mounting groove 105, thereby realizing the replacement of the water absorption unit 200.

[0025] In some embodiments, reference Figure 3 and Figure 4 Each water-absorbing unit 200 in this application includes a housing 202, a top plate 203, and a plurality of water-absorbing balls 204. Specifically, the opposite sides of the housing 202 are respectively disposed in a first mounting groove 104 and a second mounting groove 105. One side of the top plate 203 is hinged to the top of the housing 202 to allow the housing 202 to be in an open or closed state. A plurality of diffusion holes 201 are evenly provided on the bottom wall of the housing 202 and the top plate 203. The plurality of water-absorbing balls 204 are disposed in the housing 202 and their diameter is larger than the diameter of the diffusion holes 201. The fact that one side of the top plate 203 is hinged to the top of the housing 202 facilitates opening the top plate 203 to replace the water-absorbing balls 204 inside the housing 202.

[0026] In the above embodiment, monensin exhaust gas enters the dewatering tank 100 from the exhaust port of the monensin production device 300 through the first pipe 101, and diffuses from bottom to top within the dewatering tank 100. During the diffusion process, the monensin exhaust gas comes into full contact with the water-absorbing balls 204 in the multiple accommodating shells 202 inside the dewatering tank 100 from bottom to top. In this way, the water-absorbing balls 204 absorb as much moisture as possible from the monensin exhaust gas, thereby reducing the water content in the monensin exhaust gas. This avoids the situation where monensin in the monensin exhaust gas adheres to the inner wall of the cyclone separator body 400 due to high water content, thereby improving the separation efficiency and yield of monensin.

[0027] In some embodiments, the absorbent ball 204 in this application is made of silicone or calcium chloride. The silicone absorbent ball 204 can be dried and reused after it becomes ineffective, while calcium chloride has high-efficiency water absorption performance in a short period of time. In actual use, either one can be selected according to the specific circumstances.

[0028] In some embodiments, the diameter of the diffusion through-hole 201 in this application is 1mm to 3mm. If the diameter of the diffusion through-hole 201 is too small, the gas diffusion rate is slow; if the diameter is too large, the contact time between the monensin waste gas and the water absorption unit 200 is short, resulting in poor water removal efficiency by the water absorption unit 200. In other words, the diameter of the diffusion through-hole 201 needs to be within a suitable range. The diameter of the diffusion through-hole 201 used by the applicant in the monensin cyclone separation is between 1mm and 3mm. This not only ensures the efficiency of monensin diffusion but also ensures sufficient contact between the monensin waste gas and the water absorption unit 200 to remove as much water vapor as possible.

[0029] In some embodiments, reference Figure 1In this application, a vibrator 401 is provided on the outer wall of the lower section of the cyclone separator body 400.

[0030] In the above embodiments, the vibration of the vibrator 401 can cause monensin on the inner wall of the cyclone separator body 400 to fall quickly into the ash hopper of the cyclone separator body 400, thereby reducing the adhesion of monensin to the inner wall of the cyclone separator body 400 and thus achieving the separation efficiency of monensin by the cyclone separator body 400.

[0031] In some embodiments, reference Figure 1 In this application, the outlet of the cyclone separator body 400 is connected to a waste gas treatment device 501 through a third pipe 500. The waste gas treatment device 501 can be a bag filter or other equipment for further treatment of monensin waste gas. The specific waste gas treatment device 501 can be selected according to the composition of the monensin waste gas and the content of each composition, etc., and this application does not make specific limitations on it.

[0032] In addition, an induced draft fan 502 is installed on the third pipe 500.

[0033] In the above embodiment, during the cyclone separation of monensin, the induced draft fan 502 is turned on to provide diffusion power for the monensin waste gas. The monensin waste gas after water removal and cyclone separation can enter the waste gas treatment device 501 through the third pipe 500, and the monensin waste gas is further treated by the waste gas treatment device 501.

[0034] In some embodiments, reference Figure 1 In this application, the discharge port of the cyclone separator body 400 is connected to the monensin collection tank 601 through the fourth pipe 600; wherein, the fourth pipe 600 is provided with a discharge valve 602.

[0035] In the above embodiment, after the cyclone separator body 400 has been used for a period of time, the discharge valve 602 can be opened, so that the monensin deposited in the ash hopper of the cyclone separator body 400 after cyclone separation enters the monensin storage tank 601 through the fourth pipe 600, and the monensin is collected and stored through the monensin storage tank 601.

[0036] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of this application, and are not intended to limit them. Although this application has been described in detail with reference to the foregoing embodiments, those skilled in the art should understand that modifications can still be made to the technical solutions described in the foregoing embodiments, or equivalent substitutions can be made to some or all of the technical features therein. Such modifications or substitutions do not cause the essence of the corresponding technical solutions to deviate from the scope of the technical solutions of the embodiments of this application.

Claims

1. A monensin cyclone separator, characterized in that, include: A water removal tank (100) is provided with an air inlet and an air outlet, and a plurality of water absorption units (200) are arranged in sequence from top to bottom inside the water removal tank (100), and a plurality of diffusion through holes (201) are evenly opened on each water absorption unit (200). The air inlet is located on the side wall of the water removal tank (100) and is lower than the bottom water absorption unit (200), and is connected to a first pipe (101). The end of the first pipe (101) away from the water removal tank (100) is used to connect to the exhaust port of the monensin production device (300). The air outlet is located on the top of the water removal tank (100) and is connected to a second pipe (102). Cyclone separator body (400), the air inlet of the cyclone separator body (400) is connected to the end of the second pipe (102) away from the water removal tank (100), and is used to perform gas-solid separation on the waste gas containing monensin particles that has been dehydrated by the water removal tank (100) after entering it to obtain monensin particles.

2. The monensin cyclone separator according to claim 1, characterized in that, The side wall of the water removal tank (100) is sealed with a door (103). The water removal tank (100) has multiple first mounting slots (104) and multiple second mounting slots (105) respectively on its two opposite inner side walls. Each first mounting slot (104) is directly opposite a second mounting slot (105). The multiple first mounting slots (104) and multiple second mounting slots (105) correspond one-to-one with the multiple water absorption units (200).

3. The monensin cyclone separator according to claim 2, characterized in that, Each of the water-absorbing units (200) includes a housing (202), a top plate (203), and a plurality of water-absorbing balls (204); The opposite sides of the housing (202) are respectively disposed in the first mounting groove (104) and the second mounting groove (105). One side of the top plate (203) is hinged to the top of the housing (202) and used to make the housing (202) in an open or closed state. A plurality of diffusion holes (201) are evenly provided on the bottom wall of the housing (202) and the top plate (203). A plurality of water-absorbing balls (204) are disposed in the housing (202) and their diameter is larger than the diameter of the diffusion holes (201).

4. The monensin cyclone separator according to claim 3, characterized in that, The absorbent ball (204) is made of silicone or calcium chloride.

5. The monensin cyclone separator according to claim 1, characterized in that, The diameter of the diffusion through-hole (201) is 1mm to 3mm.

6. The monensin cyclone separator according to claim 1, characterized in that, A vibrator (401) is provided on the outer wall of the lower section of the cyclone separator body (400).

7. The monensin cyclone separator according to any one of claims 1 to 6, characterized in that, The outlet of the cyclone separator body (400) is connected to a waste gas treatment device (501) through a third pipe (500). An induced draft fan (502) is installed on the third pipe (500).

8. The monensin cyclone separator according to any one of claims 1 to 6, characterized in that, The discharge port of the cyclone separator body (400) is connected to a monensin collection tank (601) through a fourth pipe (600). The fourth pipe (600) is equipped with a discharge valve (602).

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