Wastewater purification treatment device for condiment production

Abstract

The application discloses a seasoning production wastewater purification treatment device, and relates to the technical field of seasoning wastewater purification treatment, which comprises a wastewater tank and a desalination mechanism, the desalination mechanism is arranged on the top of the wastewater tank, the desalination mechanism comprises a supporting leg, the supporting leg is arranged on the outer side of the wastewater tank, a landslide cone cylinder is arranged on the top of the supporting leg, a plurality of connecting blocks are arranged on the outer side of the landslide cone cylinder, an outer cylinder is arranged on the outer side of the connecting blocks, a cylinder cover is arranged on the top of the outer cylinder and the connecting blocks, the wastewater is collected in the collecting bin through the landslide cone cylinder, the scraper is used to scrape the crystals on the wall of the bin, the filter plate is used for secondary filtration to prevent the spray head from being blocked, the high-pressure spray head is used for back flushing to clean the filter plate and prevent the filter plate from being blocked, the wastewater is rapidly purified through the simplified steps and the accelerated evaporation and vaporization process, the overall purification time is reduced, and the purification work can be well completed under the condition that rapid filtration is required.

Description

Technical Field

[0001] This invention relates to the field of wastewater purification and treatment technology for condiment production, specifically to a wastewater purification and treatment device for condiment production. Background Technology

[0002] Seasonings are a general term for substances used in food processing or food preparation to adjust the flavor, improve the taste, enhance the color, or help preserve the freshness of food. They include basic seasonings such as salt, sugar, vinegar, and soy sauce; spices such as chili peppers, Sichuan peppercorns, and star anise; and compound seasonings such as monosodium glutamate, chicken essence, oyster sauce, and sauces. By giving food flavors such as salty, sweet, sour, spicy, and umami, they satisfy different dietary needs and flavor preferences.

[0003] Wastewater purification and treatment equipment is an integrated system that uses a combination of physical, chemical, and biological processes to classify and treat various types of wastewater, including domestic and industrial wastewater. It typically includes modules for pretreatment, core treatment, advanced treatment, and sludge treatment. It can effectively remove pollutants such as suspended solids, organic matter, nitrogen, phosphorus, and heavy metals from wastewater, ensuring that the effluent meets discharge standards or reuse requirements, and achieving the harmless disposal and recycling of water resources.

[0004] However, the existing wastewater purification and treatment device for condiment production has the following shortcomings: Wastewater from condiment production differs from ordinary domestic wastewater, characterized by high pollutant concentrations, complex composition, and large fluctuations in water quality and quantity. It is often accompanied by high salt and high color, especially in the production of soy sauce and pickles, where the wastewater contains a large amount of sodium chloride. Currently available wastewater purification devices for condiment production involve more treatment steps due to the characteristics of condiment wastewater. In the desalination stage, evaporation is usually used to crystallize salt, making the entire wastewater treatment process relatively slow and increasing the overall working time. In some cases where rapid filtration is required, the above methods are insufficient.

[0005] Therefore, this invention proposes a wastewater purification and treatment device for condiment production, in order to solve the problems mentioned above. Summary of the Invention

[0006] The purpose of this invention is to provide a wastewater purification and treatment device for condiment production. Pre-treated wastewater is discharged into a wastewater tank and then pumped to a nozzle water supply chamber by a waterproof pump. A primary filter head simultaneously performs primary filtration to prevent impurities from entering the pump. The wastewater is atomized into a spray by the nozzle module. The high-temperature chamber maximizes the contact area of ​​the droplets and shortens the vaporization path. The humidity difference accelerates water diffusion, causing the salt concentration to rise rapidly and crystallize. The crystals fall onto the salt plate by gravity. Viscous water droplets also undergo secondary drying and crystallization on the salt plate. A first motor drives the rotating frame, filter plate, and scraper to operate synchronously. A first pusher moves the salt plate... The central crystals are pushed outwards, and a ring linear motor drives a second motor to revolve around the central axis. The second pusher bar rotates synchronously, pushing the crystals away from the salt plate and sliding down the slide cone into the collection chamber. At the same time, a scraper removes the crystals adhering to the chamber wall, the filter plate performs secondary filtration to prevent nozzle clogging, and the high-pressure nozzle back-blowing cleans the filter plate to ensure continuous operation. A force compensation frame supports the second pusher bar to prevent tilting and deformation, and the device cover seals the high-temperature chamber to reduce heat loss. The overall solution omits intermediate transfer links, simplifies the structure, accelerates vaporization efficiency, reduces maintenance costs and energy consumption, and can quickly complete wastewater purification, adapting to the needs of rapid filtration.

[0007] To achieve the above objectives, the present invention provides the following technical solution: a wastewater purification and treatment device for condiment production, comprising a wastewater tank and a desalination mechanism, wherein the desalination mechanism is disposed on the top of the wastewater tank; The desalination mechanism includes support legs disposed on the outside of the wastewater tank. A landslide cone is mounted on the top of the support legs. Multiple connecting blocks are disposed on the outside of the landslide cone. An outer cylinder is mounted on the outside of the multiple connecting blocks. A cylinder cover is mounted on the top of the outer cylinder and the connecting blocks. A nozzle bracket is mounted on the inside of the wastewater tank. A waterproof water pump is mounted on the bottom inside the wastewater tank. A filter head is mounted on the input end of the waterproof water pump. A salt plate is mounted on the top of the wastewater tank. The salt plate is located on top of the nozzle bracket.

[0008] Preferably, a water supply chamber for the nozzle is installed on the top of the nozzle bracket, and the bottom input end of the water supply chamber for the nozzle is connected to the top output end of the waterproof water pump.

[0009] Preferably, the salt plate is sleeved on the outside of the nozzle water supply chamber, the inside of the nozzle water supply chamber is provided with a filter groove, and the top of the nozzle water supply chamber is connected to the nozzle module.

[0010] Preferably, a filter plate is rotatably connected to the inner side of the filter tank, and the filter plate is located on top of the salt plate.

[0011] Preferably, a device cover is installed on the top of the cylinder cover, a high-temperature chamber is installed on the inner side of the top of the device cover, and a first motor is installed on the top of the high-temperature chamber.

[0012] Preferably, the bottom output end of the first motor passes through the high-temperature chamber and is equipped with a connecting rod. The other end of the connecting rod is installed on the top of the filter plate. A rotating frame is installed in the middle of the outer side of the connecting rod. A first lever is installed at the bottom of the rotating frame. The first lever is located on the top surface of the salt plate.

[0013] Preferably, a ring linear motor is installed on the outside of the high-temperature chamber, a dustproof chamber is installed on the outside of the ring linear motor, and a second motor is installed on the inside of the dustproof chamber.

[0014] Preferably, a second lever is installed at the bottom output end of the second motor, the second lever is located on the top surface of the salt plate, and the annular linear motor and the dustproof chamber are located inside the device cover.

[0015] Preferably, a first scraper is installed on the top outer side of the connecting rod, and a plurality of second scrapers are installed on the outer side of the first scraper. The first scraper is located on the top inner wall of the high-temperature chamber, and the second scrapers are located on the surrounding inner walls of the high-temperature chamber. A force compensation frame is installed on the top of the landslide cone, and the force compensation frame is located at the bottom of the second lever.

[0016] Preferably, a booster air pump is installed on the outside of the device cover, and the output end of the booster air pump is connected to an air supply pipe. The other end of the air supply pipe passes through the device cover, the high-temperature chamber, and the salt plate and is connected to a high-pressure nozzle. The high-pressure nozzle is located on the top of the filter plate, and a collection chamber is provided on the outside of the support leg.

[0017] Compared with the prior art, the beneficial effects of the present invention are: 1. In this invention, during desalination, pretreated wastewater is discharged into a wastewater tank and pumped into a nozzle supply chamber via a waterproof pump. A filter head simultaneously filters to prevent impurities from entering. The wastewater is sprayed into a mist by the nozzle module. High-temperature vaporization occurs in the high-temperature chamber, resulting in a large droplet contact area, a short vaporization path, and humidity differences that promote water diffusion. As the salt concentration increases, rapid crystallization occurs, and the crystals fall onto the salt plate under gravity. Viscous water droplets also undergo secondary drying and crystallization on the salt plate. A first motor drives the scraper, rotating frame, and filter plate to rotate. A first deflector pushes the crystals in the center of the salt plate to the surrounding areas. A circular linear motor drives a second motor to rotate around the high-temperature chamber. The second deflector rotates on its own axis and revolves around the center, pushing the crystals away from the salt plate. The crystals slide down a ramp cone into a collection chamber. The scraper removes the crystals from the chamber wall, and the filter plate performs secondary filtration to prevent nozzle clogging. A high-pressure nozzle backflush cleans the filter plate, preventing blockage. This simplified process and accelerated evaporation and vaporization achieve rapid wastewater purification, reducing overall purification time and enabling efficient purification in situations requiring rapid filtration.

[0018] 2. The force compensation frame in the device of this invention supports the second lever to prevent it from tilting due to insufficient bottom support during rotation. It also compensates for the bending moment generated by revolution and rotation, preventing long-term deformation under stress, extending component lifespan, and ensuring salt collection stability. The gap between the high-temperature chamber and the cylinder cover allows for movement of the second motor output end. The device cover seals the high-temperature chamber to reduce heat loss. The device atomizes the pre-treated wastewater through the nozzle module, achieving rapid vaporization and crystallization in conjunction with the high-temperature chamber. The crystals fall onto the salt plate by gravity, eliminating the crystal slurry transport and solid-liquid separation steps, reducing salt crystallization transport losses, accelerating the vaporization process, and improving recovery efficiency. The primary filter head filters the inlet water to prevent impurities from entering the waterproof water pump. The rotating filter... The secondary dynamic filter nozzle water supply chamber prevents nozzle clogging, and the high-pressure nozzle back-blowing cleans the filter plate without requiring shutdown and disassembly, ensuring continuous operation of the device and reducing maintenance costs. The first scraper rotates with the rotating frame to push the crystals in the middle of the salt plate to the surrounding area, while the second scraper revolves around the high-temperature chamber and rotates on its own axis under the drive of a ring linear motor. The linkage of the two scrapers enables rapid and automatic collection of salt crystals, which improves salt collection efficiency compared to the traditional single scraper and avoids crystal accumulation and clumping. The first and second scrapers share the same drive source with the filter plate and the first scraper, and coaxially link to scrape off the salt crystals adhering to the inner wall of the high-temperature chamber, achieving self-cleaning without the need for an additional cleaning drive mechanism, simplifying the device structure and reducing energy consumption and failure rate. Attached Figure Description

[0019] Figure 1 This is a perspective view of the main structure of a wastewater purification and treatment device for condiment production according to the present invention. Figure 2 This is a three-dimensional, exploded view of the structure of a wastewater purification and treatment device for condiment production according to the present invention. Figure 3 This is a demonstration of the location of the desalination mechanism in a wastewater purification and treatment device for condiment production according to the present invention; Figure 4 This is a split perspective view of the desalination mechanism in a wastewater purification and treatment device for condiment production according to the present invention. Figure 5 for Figure 4 Enlarged view of point A in the image; Figure 6 for Figure 4 Enlarged view of point B in the image; Figure 7 This is a partially exploded perspective view of the desalination mechanism in a wastewater purification and treatment device for condiment production according to the present invention. Figure 8 for Figure 7 Enlarged view of point C in the image; Figure 9 This is a structural diagram illustrating the various parts of a wastewater purification and treatment device for condiment production according to the present invention.

[0020] In the diagram: 1. Wastewater tank; 2. Desalination mechanism; 201. Support leg; 202. Landslide cone; 203. Outer cylinder; 204. Connecting block; 205. Cylinder cover; 206. Device cover; 207. High-temperature chamber; 208. First motor; 209. Waterproof pump; 210. Filter head; 211. Nozzle bracket; 212. Nozzle water supply chamber; 213. Nozzle module; 214. Filter tank; 215. Salt plate; 216. Filter plate; 217. Rotating frame; 218. First lever; 219. High-pressure nozzle; 220. Air supply pipe; 221. Booster pump; 222. Circular linear motor; 223. Dustproof chamber; 224. Second motor; 225. Second lever; 226. First scraper; 227. Second scraper; 228. Collection chamber; 229. Connecting rod; 230. Force compensation frame. Detailed Implementation

[0021] The technical solutions of the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some embodiments of the present invention, and not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of the present invention.

[0022] Example 1, according to Figures 1-3 As shown, a wastewater purification device for condiment production includes a wastewater tank 1 and a desalination mechanism 2. The desalination mechanism 2 is located on top of the wastewater tank 1 and includes support legs 201 located on the outside of the wastewater tank 1. A landslide cone 202 is mounted on the top of the support legs 201. Multiple connecting blocks 204 are arranged on the outside of the landslide cone 202. An outer cylinder 203 is mounted on the outside of the multiple connecting blocks 204. A cylinder cover 205 is mounted on the top of the outer cylinder 203 and the connecting blocks 204. A nozzle bracket 211 is mounted on the inside of the wastewater tank 1. A waterproof water pump 209 is installed on the bottom inner side. A filter head 210 is installed at the input end of the waterproof water pump 209. A salt plate 215 is installed on the top of the wastewater tank 1. The salt plate 215 is located on the top of the nozzle support 211. A nozzle water supply chamber 212 is installed on the top of the nozzle support 211. The bottom input end of the nozzle water supply chamber 212 is connected to the top output end of the waterproof water pump 209. The salt plate 215 is sleeved on the outside of the nozzle water supply chamber 212. A filter groove 214 is opened on the inner side of the nozzle water supply chamber 212. A nozzle module 213 is connected to the top of the nozzle water supply chamber 212.

[0023] The overall effect of Embodiment 1 is as follows: When the wastewater is desalinated, the wastewater after sedimentation and filtration is first discharged into the wastewater tank 1, and then sent to the nozzle water supply chamber 212 by the waterproof water pump 209. The filter head 210 simultaneously filters the wastewater entering the waterproof water pump 209 to prevent impurities from entering. The wastewater is sprayed into a mist from the nozzle module 213 through the nozzle water supply chamber 212. The high-temperature chamber 207 vaporizes the mist at high temperature, maximizing the contact area between the spray droplets and the high-temperature environment, shortening the water vaporization path, and reducing the relative humidity of the surrounding environment to create a humidity difference, which promotes the diffusion of water droplets into the air and avoids the accumulation of water vapor that hinders vaporization. Moisture rapidly diffuses to the surface, causing the salt concentration to rise sharply. Once the solubility exceeds the limits at high temperatures, salt crystals rapidly form inside and on the surface of the droplets. After complete vaporization, the droplets form dry salt crystal particles, which fall onto the top of the salt plate 215 under gravity. If these crystal particles encounter vaporized steam, they form viscous water droplets that fall onto the surface of the salt plate 215. Because the high-temperature chamber 207 is a high-temperature zone, the brine mixture re-dries and crystallizes on the surface of the salt plate 215, causing the salt crystals on the top of the salt plate 215 to gradually increase. The continuously running first motor 208 drives the first scraper 226, the rotating frame 217, and the filter plate 216 to rotate synchronously via the connecting rod 229. 17 drives the first scraper 218 to rotate, pushing the salt crystals in the center of the top of the salt plate 215 to the surrounding areas. The annular linear motor 222 drives the second motor 224 to rotate around the high-temperature chamber 207. The second motor 224 simultaneously drives the second scraper 225 to rotate, causing the second scraper 225 to rotate around the high-temperature chamber 207 while rotating on its own axis. This pushes the salt crystals pushed to the surrounding areas by the first scraper 218 away from the salt plate 215 and onto the surface of the landslide cone 202. The salt crystals slide down the landslide surface of the landslide cone 202 to the space between the landslide cone 202 and the outer cylinder 203, and finally fall into the collection chamber 228, completing the evaporation and desalination process. The continuously rotating first scraper 226 and... The second scraper 227 adheres to the inner surface of the high-temperature chamber 207, scraping off the adhering salt crystals to the top of the salt plate 215. The rotating filter plate 216 filters the wastewater from the nozzle water supply chamber 212 to the nozzle module 213 again, preventing the nozzle module 213 from clogging. During the rotation, the filter plate 216 continuously comes into alternating contact with the sewage and the high-pressure nozzle 219. When in contact with the high-pressure nozzle 219, the booster pump 221 delivers high-pressure airflow to the high-pressure nozzle 219 through the air supply pipe 220. The high-pressure nozzle 219 sprays the high-pressure airflow onto the surface of the filter plate 216, spraying the filtered and intercepted dirt onto the surface of the salt plate 215, thus preventing the filter plate 216 from clogging.

[0024] Example 2, according to Figures 4-9As shown, a filter plate 216 is rotatably connected to the inner side of the filter tank 214. The filter plate 216 is located on top of the salt plate 215. A device cover 206 is installed on the top of the cylinder cover 205. A high-temperature chamber 207 is installed on the inner side of the top of the device cover 206. A first motor 208 is installed on the top of the high-temperature chamber 207. The bottom output end of the first motor 208 passes through the high-temperature chamber 207 and is connected to a connecting rod 229. The other end of the connecting rod 229 is installed on the top of the filter plate 216. A rotating frame 217 is installed in the middle of the outer side of the connecting rod 229. A first lever 218 is installed at the bottom of the rotating frame 217. The first lever 218 is located on the top surface of the salt plate 215. A ring linear motor 222 is installed on the outer side of the high-temperature chamber 207. A dustproof chamber 223 is installed on the outer side of the ring linear motor 222. A second motor 224 is installed inside the dustproof chamber 223. A second lever 224 is installed at the bottom output end of the second motor 224. 25. The second lever 225 is located on the top surface of the salt plate 215. The annular linear motor 222 and the dustproof chamber 223 are located inside the device cover 206. The top of the outer side of the connecting rod 229 is equipped with a first scraper 226. Multiple second scrapers 227 are installed on the outer side of the first scraper 226. The first scraper 226 is located on the top inner wall of the high temperature chamber 207. The second scrapers 227 are located on the inner walls around the high temperature chamber 207. The top of the landslide cone 202 is equipped with a force compensation frame 230. The force compensation frame 230 is located at the bottom of the second lever 225. The outer side of the device cover 206 is equipped with a booster air pump 221. The output end of the booster air pump 221 is connected to an air supply pipe 220. The other end of the air supply pipe 220 passes through the device cover 206, the high temperature chamber 207, and the salt plate 215 and is connected to a high pressure nozzle 219. The high pressure nozzle 219 is located on the top of the filter plate 216. A collection chamber 228 is provided on the outer side of the support leg 201.

[0025] The overall effect of Embodiment 2 is as follows: the force compensation frame 230 supports the second lever 225, preventing the second lever 225 from tilting due to insufficient bottom support during rotation; the gap between the high-temperature chamber 207 and the cylinder cover 205 allows the output end of the second motor 224 to move within it; the device cover 206 is used to seal the high-temperature chamber 207 to reduce heat loss; the device atomizes the pretreated wastewater into a spray through the nozzle module 213, achieving rapid vaporization and crystallization in combination with the high-temperature environment of the high-temperature chamber 207; the crystals fall directly onto the salt plate 215 by gravity, which, compared to the traditional evaporation crystallization process, eliminates the need for crystallization. The intermediate steps of slurry conveying and solid-liquid separation reduce salt crystallization transport losses, accelerate the evaporation and vaporization process, and improve salt recovery efficiency. Filter head 210 performs primary filtration of the inlet water to prevent large particles from entering the waterproof water pump 209. The rotating filter plate 216 performs secondary dynamic filtration of the water outlet from the nozzle water supply chamber 212 to prevent clogging of the nozzle module 213. At the same time, the high-pressure nozzle 219 backflushes and cleans the filter plate 216 without requiring shutdown for disassembly and cleaning, ensuring continuous operation of the device and reducing maintenance costs. The first and second guide bars 218 work together to collect salt crystals, achieving salt crystallization... The rapid and automatic collection of salt crystals involves the first scraper 218 rotating with the rotating frame 217, pushing the salt crystals in the center of the salt plate 215 to the surrounding areas. The second scraper 225, driven by a circular linear motor 222, revolves around the high-temperature chamber 207 while simultaneously rotating on its own axis, rapidly pushing the salt crystals around the salt plate 215 away from the plate. Compared to traditional single-scraper salt collection, the linkage of the two scrapers improves salt collection efficiency and prevents salt crystals from accumulating and agglomerating on the surface of the salt plate 215. The scraper and the scraper are coaxially linked, achieving self-cleaning of the inner wall of the high-temperature chamber 207. The first scraper 226, the second scraper 227, the filter plate 216, and the first scraper 225... The 18 components share the same drive source, simultaneously scraping away salt crystals adhering to the inner wall of the high-temperature chamber 207 while rotating the filter plate 216 and agitating the salt crystals. This eliminates the need for an additional cleaning drive mechanism, simplifying the device structure and reducing energy consumption and failure rate. The force compensation frame 230 ensures the long-term stable operation of the second agitator 225. Located at the bottom of the second agitator 225, the force compensation frame 230 supports and compensates for the bending moment generated during the revolution and rotation of the second agitator 225, effectively preventing deformation of the second agitator 225 due to long-term stress, extending the service life of the components, and ensuring the stability of the salt collection effect.

[0026] The working principle of the entire device is as follows: When the wastewater desalination treatment begins, the wastewater after sedimentation and filtration is first discharged into the wastewater tank 1. The wastewater is then carried into the nozzle water supply chamber 212 by the waterproof water pump 209. During this period, the filter head 210 further filters the water entering the waterproof water pump 209 to prevent impurities from entering the pump. The wastewater passes through the nozzle water supply chamber 212 until it is sprayed outwards from the nozzle module 213. At this time, the high-temperature chamber 207 vaporizes the spray through high temperature. This method maximizes the contact area between the spray droplets and the high-temperature environment, shortens the vaporization path of the water, and simultaneously reduces the relative humidity of the surrounding environment, creating a higher humidity difference, which further promotes the diffusion of water droplets into the air. To prevent water vapor from accumulating around the droplets and hindering further vaporization, the water inside the spray droplets rapidly diffuses to the surface, causing a sharp increase in salt concentration within the droplets. When the salt concentration exceeds its solubility at high temperatures, salt crystals rapidly form both inside and on the surface of the spray droplets. Eventually, the droplets completely vaporize, forming dry salt crystal particles that fall to the top of the salt plate 215 under gravity. During this process, when the crystal particles encounter other vaporized steam, they fall as viscous water droplets onto the top surface of the salt plate 215. However, because the entire high-temperature chamber 207 is a high-temperature zone, the brine mixture in this state gradually loses moisture on the surface of the salt plate 215 and dries and crystallizes again. Through this process, the amount of salt crystals on the top of the salt plate 215 gradually increases. At this point, the process continues. The first motor 208 drives the first scraper 226, the rotating frame 217, and the filter plate 216 to rotate synchronously via the connecting rod 229. The rotating frame 217 drives the first deflector 218 to rotate, pushing the salt crystals in the middle of the top of the salt plate 215 to the periphery of the salt plate 215. At this time, the annular linear motor 222 drives the second motor 224 to rotate around the high-temperature chamber 207. During the rotation, the second motor 224 drives the second deflector 225 to rotate. Thus, the second deflector 225 rotates around the high-temperature chamber 207 while rotating on its own axis. During this process, the second deflector 225 pushes the salt crystals pushed to the periphery by the first deflector 218 away from the surface of the salt plate 215 and onto the surface of the landslide cone 202. Because the surface of the landslide cone 202 is landslide-shaped... Salt crystals slide down the landslide cone 202 and the outer cylinder 203, eventually falling into the collection chamber 228, thus completing the evaporation and desalination process. The continuously rotating first scraper 226 and second scraper 227 adhere to the inner surface of the high-temperature chamber 207, scraping the salt crystals adhering to the inner surface of the high-temperature chamber 207 onto the top of the salt plate 215. The rotating filter plate 216 further filters the water flowing from the nozzle supply chamber 212 to the nozzle module 213, preventing clogging. The continuously rotating filter plate 216 alternately contacts the wastewater and the high-pressure nozzle 219. When in contact with the high-pressure nozzle 219, the booster pump 221 delivers high-pressure airflow through the air pipe 220 to the high-pressure nozzle 219.This causes the high-pressure nozzle 219 to spray high-pressure airflow onto the top surface of the filter plate 216, thus spraying the filtered and intercepted dirt inside the filter plate 216 onto the surface of the salt plate 215, preventing the filter plate 216 from becoming clogged.

[0027] Although the present invention has been described in detail with reference to the foregoing embodiments, those skilled in the art can still modify the technical solutions described in the foregoing embodiments or make equivalent substitutions for some of the technical features. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of the present invention should be included within the protection scope of the present invention.

Claims

1. A wastewater purification and treatment device for condiment production, characterized in that: It includes a wastewater tank (1) and a desalination mechanism (2), wherein the desalination mechanism (2) is disposed on the top of the wastewater tank (1); The desalination mechanism (2) includes a support leg (201) located on the outside of the wastewater tank (1). A landslide cone (202) is mounted on the top of the support leg (201). Multiple connecting blocks (204) are provided on the outside of the landslide cone (202). An outer cylinder (203) is mounted on the outside of the multiple connecting blocks (204). A cylinder cover (205) is mounted on the top of the outer cylinder (203) and the connecting blocks (204). A nozzle bracket (211) is mounted on the inside of the wastewater tank (1). A waterproof water pump (209) is installed at the bottom inner side of the wastewater tank (1). A filter head (210) is installed at the input end of the waterproof water pump (209). A salt plate (215) is installed on the top of the wastewater tank (1). The salt plate (215) is located on the top of the nozzle support (211). A nozzle water supply chamber (212) is installed on the top of the nozzle support (211). The bottom input end of the nozzle water supply chamber (212) is connected to the top output end of the waterproof water pump (209). The salt plate (210) is installed on the bottom inner side of the wastewater tank (1). 15) The nozzle water supply chamber (212) is fitted on the outside of the nozzle water supply chamber (212). A filter groove (214) is provided on the inside of the nozzle water supply chamber (212). The top of the nozzle water supply chamber (212) is connected to the nozzle module (213). A filter plate (216) is rotatably connected to the inside of the filter groove (214). The filter plate (216) is located on the top of the salt plate (215). A device cover (206) is installed on the top of the cylinder cover (205). A high-temperature chamber (207) is installed on the inside of the top of the device cover (206). A first motor (208) is installed on the top of the high-temperature chamber (207). The bottom output end of the first motor (208) passes through the high-temperature chamber (207) and is equipped with a connecting rod (229). The other end of the connecting rod (229) is installed on the top of the filter plate (216). A rotating frame (217) is installed in the middle of the outer side of the connecting rod (229). A first lever (218) is installed at the bottom of the rotating frame (217). The first lever (218) is located on the top surface of the salt plate (215).

2. The wastewater purification and treatment device for condiment production according to claim 1, characterized in that: A ring linear motor (222) is installed on the outside of the high-temperature chamber (207). A dustproof chamber (223) is installed on the outside of the ring linear motor (222). A second motor (224) is installed on the inside of the dustproof chamber (223). A second lever (225) is installed at the bottom output end of the second motor (224). The second lever (225) is located on the top surface of the salt plate (215). The ring linear motor (222) and the dustproof chamber (223) are located inside the device cover (206).

3. The wastewater purification and treatment device for condiment production according to claim 2, characterized in that: A first scraper (226) is installed on the top outer side of the connecting rod (229), and a plurality of second scrapers (227) are installed on the outer side of the first scraper (226). The first scraper (226) is located on the top inner wall of the high temperature chamber (207), and the second scrapers (227) are located on the inner walls around the high temperature chamber (207). A force compensation frame (230) is installed on the top of the landslide cone (202), and the force compensation frame (230) is located at the bottom of the second lever (225).

4. The wastewater purification and treatment device for condiment production according to claim 3, characterized in that: A booster pump (221) is installed on the outside of the device cover (206). The output end of the booster pump (221) is connected to a gas supply pipe (220). The other end of the gas supply pipe (220) passes through the device cover (206), the high temperature chamber (207), and the salt plate (215) and is connected to a high pressure nozzle (219). The high pressure nozzle (219) is located on the top of the filter plate (216). A collection chamber (228) is provided on the outside of the support leg (201).

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