Rapid treatment device for high-concentration ammonia-nitrogen wastewater

Abstract

The invention discloses a high-concentration ammonia-nitrogen wastewater rapid treatment device, and relates to the technical field of sewage treatment.The high-concentration ammonia-nitrogen wastewater rapid treatment device comprises a device body, a main box body and a side box assembly, the side box assembly comprises a stirring box body A and a stirring box body B, and the stirring box body A and the stirring box body B are located on the two sides of the main box body respectively; the device main body comprises a heating assembly for accelerating volatilization, a gas-liquid separation assembly connected with the heating assembly, and a stirring assembly connected with the gas-liquid separation assembly. The ammonia-nitrogen wastewater gas-liquid separation device has the advantages that the two cyclone separators and the two stirring rods are driven by the motor to perform stirring while performing gas-liquid separation on ammonia-nitrogen wastewater; at the moment, the steam enters the treatment box to generate ammonium salt, an arranged concentration sensor is matched, so that the ammonia-nitrogen wastewater is conveniently treated and stirred according to the separation state of the gas-liquid separation assembly, gas-liquid separation is thorough, the treatment load of the ammonia-nitrogen stirring assembly is reduced, and the treatment efficiency of ammonia nitrogen is improved.

Description

Technical Field

[0001] The present invention relates to the technical field of sewage treatment, and specifically to a rapid treatment device for high-concentration ammonia-nitrogen wastewater. Background Art

[0002] Ammonia-nitrogen wastewater refers to wastewater containing excessive ammonia-nitrogen compounds, which is commonly found in many industries such as chemical engineering, pharmaceuticals, fertilizers, aquaculture, and landfill leachate treatment. With the rapid development of industry and the continuous growth of the population, if high-concentration ammonia-nitrogen wastewater is directly discharged without effective treatment, it will cause a series of environmental problems. On the one hand, ammonia-nitrogen will consume a large amount of dissolved oxygen in the water body, leading to eutrophication of the water body, promoting the massive reproduction of plankton such as algae, forming water blooms or red tides, destroying the balance of the aquatic ecosystem, and causing aquatic organisms such as fish to die due to lack of oxygen. On the other hand, ammonia-nitrogen will be converted into nitrite and nitrate under certain conditions. Nitrite is toxic and can combine with hemoglobin in the human body to form methemoglobin, reducing the oxygen-carrying capacity of the blood and endangering human health. The discharge volume of high-concentration ammonia-nitrogen wastewater is increasing day by day, posing a serious threat to the ecological environment and human health;

[0003] Existing ammonia-nitrogen wastewater treatment devices cannot be combined with the ammonia-nitrogen stirring mechanism according to the separation state of the gas-liquid separation device, resulting in incomplete gas-liquid separation, causing liquid containing a high concentration of ammonia-nitrogen to enter the subsequent treatment link, increasing the treatment load of the ammonia-nitrogen stirring mechanism, and reducing its treatment efficiency and effect on ammonia-nitrogen. Furthermore, it cannot meet the increasingly strict environmental protection requirements and complex and changeable wastewater treatment conditions. Therefore, we propose a rapid treatment device for high-concentration ammonia-nitrogen wastewater. Summary of the Invention

[0004] The purpose of the present invention is to provide a rapid treatment device for high-concentration ammonia-nitrogen wastewater.

[0005] To achieve the above object, the present invention provides the following technical solution: A rapid treatment device for high-concentration ammonia-nitrogen wastewater, comprising a device main body, a main box body, and a side box assembly. The side box assembly includes a stirring box body A and a stirring box body B, and the stirring box body A and the stirring box body B are respectively located on both sides of the main box body. It is characterized in that: The device main body includes a heating component for accelerating volatilization, a gas-liquid separation component connected to the heating component, and a stirring component connected to the gas-liquid separation component. The gas-liquid separation component includes a motor and a transmission box body one. On both of the two motors, a cyclone separator is arranged through a rotating shaft. The gas-liquid separation component is arranged inside the transmission box body one. The heating component includes a jacket, an internal heating kettle, and a heating pipe. The internal heating kettle is arranged inside the jacket. The two motors are respectively connected to a compressor. A condenser is arranged on the compressor. An evaporator and an expansion valve are sequentially arranged from top to bottom on the left side of the condenser. The compressor, the condenser, the expansion valve, and the evaporator are all connected through the heating pipe to form a closed circulation system. The stirring component includes a stirring rod, stirring blades, and a transmission belt. A plurality of the stirring blades are arranged on the stirring rod. The two ends of the transmission belt are respectively arranged on the stirring rod and the rotating shaft.

[0006] As a further scheme of the present invention: The heating component is arranged in two, and is evenly distributed on both sides of the main box body. The stirring component is arranged in two, and is respectively located inside the stirring box body A and the stirring box body B. The stirring box body A, the stirring box body B, and the main box body penetrate each other. A transmission box body two is arranged on the transmission belt and the stirring rod.

[0007] As a further scheme of the present invention: A treatment component is arranged inside the main box body. The treatment component includes a treatment box and a liquid storage tank. The treatment box is arranged at the inner top of the main box body. The liquid storage tank is arranged on the top surface of the main box body. A liquid inlet is arranged on the liquid storage tank. The bottom of the liquid storage tank is connected to a liquid collecting plate through a pipeline. Several liquid outlet pipes are arranged at the bottom of the liquid collecting plate. The pipeline, the liquid collecting plate, and the liquid outlet pipes are all arranged inside the treatment box.

[0008] As a further scheme of the present invention: On both outer walls of the treatment box, an outlet is opened. The outlet penetrates through the outer walls of the treatment box and the main box body. A check valve three is arranged on the outlet.

[0009] As a further scheme of the present invention: A circulation component is arranged behind the device main body. The circulation component includes a circulation pipe. A water inlet pipe is arranged behind the internal heating kettle and the jacket. The water inlet pipe is communicated with the heating pipe. One end of the circulation pipe is connected to the main box body, and the other end is connected to the water inlet pipe, and the circulation pipe is communicated with the water inlet pipe. A pressure sensor and a micro pump two are sequentially arranged from top to bottom on the circulation pipe.

[0010] As a further solution of the present invention: a micro pump I is provided on the water inlet pipe, and discharge pipes are provided on both sides of the stirring box body A and the stirring box body B.

[0011] As a further solution of the present invention: a connecting pipe is provided at the bottom of the jacket and the internal heating kettle, and a check valve I is provided on the connecting pipe.

[0012] As a further solution of the present invention: an air inlet pipe is provided between the treatment box and the jacket, and a check valve II is provided on the air inlet pipe.

[0013] As a further solution of the present invention: a temperature sensor is provided inside the internal heating kettle, a concentration sensor is provided inside the main box body, and a controller is provided in front of the device main body. The controller is electrically connected to the pressure sensor, the temperature sensor, the concentration sensor, the motor, the micro pump I, and the micro pump II respectively.

[0014] Adopting the above technical solutions, compared with the prior art, the beneficial effects of the present invention are as follows:

[0015] 1. In the present invention, the motor drives the two cyclone separators and the two stirring rods to stir while performing gas-liquid separation on the ammonia nitrogen wastewater. At this time, steam enters the treatment box to generate ammonium salts. With the concentration sensor provided, it is convenient to treat and stir the ammonia nitrogen wastewater according to the separation state of the gas-liquid separation component. The gas-liquid separation is thorough, reducing the treatment load of the ammonia nitrogen stirring component, improving the treatment efficiency of ammonia nitrogen, and meeting the increasingly strict environmental protection requirements and complex and changeable wastewater treatment conditions.

[0016] 2. In the present invention, the compressor, condenser, expansion valve, and evaporator in the heating component are used to heat the wastewater entering the hot water pipe. With the temperature sensor provided to sense the temperature inside the internal heating kettle in real time, it is convenient for the ammonia nitrogen wastewater treatment device to operate continuously and efficiently, realizing the rapid and accurate treatment of high-concentration ammonia nitrogen wastewater.

[0017] 3. In the present invention, by setting the treatment component, when steam enters the treatment box, the washing liquid containing acidic substances is sprayed through the liquid outlet pipe, and ammonia nitrogen reacts with the acidic substances to form ammonium salts, which are thus absorbed by the washing liquid. The ammonia nitrogen in the steam is efficiently converted into ammonium salts and absorbed, realizing the effective removal of ammonia nitrogen.

[0018] 4. By providing the circulation pipe and the second micro pump in the circulation component, and cooperating with the provided pressure sensor in the present invention, it is convenient to restart the second micro pump to enter the water inlet pipe for processing again. The pressure sensor monitors the pressure in the circulation pipe in real time. Through the heating processes in the internal heating kettle and the jacket, the separation by the gas-liquid separation component, and the stirring by the stirring component, etc., until the concentration of ammonia-nitrogen particles in the main box reaches the expected standard. Through the coordinated cooperation and precise control of each component, the efficient and stable treatment of high-concentration ammonia-nitrogen wastewater is achieved, ensuring that the treatment effect meets the environmental protection requirements and the actual application needs.

[0019] Other advantages, objectives, and features of the present invention will be described to some extent in the subsequent description, and to some extent, will be obvious to those skilled in the art based on the study of the following text, or can be learned from the practice of the present invention. BRIEF DESCRIPTION OF THE DRAWINGS

[0020] Figure 1 is the first three-dimensional schematic diagram of the embodiment of the present invention;

[0021] Figure 2 is the second three-dimensional schematic diagram of the embodiment of the present invention;

[0022] Figure 3 is the third three-dimensional schematic diagram of the embodiment of the present invention;

[0023] Figure 4 is the connection structure schematic diagram of the connecting pipe, the treatment component, and the liquid outlet pipe in the embodiment of the present invention;

[0024] Figure 5 is Figure 4 the schematic diagram at position B in

[0025] Figure 6 is the schematic diagram of the heating component in the embodiment of the present invention;

[0026] Figure 7 is the schematic diagram of the circulation component in the embodiment of the present invention;

[0027] Figure 8 is the connection structure schematic diagram of the stirring component, the transmission box, and the cyclone separator in the embodiment of the present invention;

[0028] Figure 9 is Figure 8 the schematic diagram at position A in

[0029] Figure 10 is the schematic diagram of the treatment component and the liquid storage tank in the embodiment of the present invention.

[0030] In the figure: 1. Device main body; 2. Main box body; 3. Side box assembly; 31. Stirring box body A; 32. Stirring box body B; 4. Water inlet pipe; 5. Heating assembly; 51. Jacket; 52. Inner heating kettle; 53. Heating pipe; 54. Compressor; 55. Condenser; 56. Expansion valve; 57. Evaporator; 6. Gas-liquid separation assembly; 61. Motor; 62. Transmission box body one; 63. Cyclone separator; 7. Connecting pipe; 9. Transmission box body two; 8. Stirring assembly; 81. Stirring rod; 82. Stirring blade; 83. Transmission belt; 10. Air inlet pipe; 11. Treatment assembly; 111. Treatment box; 112. Liquid storage tank; 113. Liquid collecting plate; 114. Liquid outlet pipe; 12. Outlet; 13. Circulation assembly; 131. Circulation pipe; 132. Micro pump two; 133. Pressure sensor; 14. Discharge pipe. Specific embodiments

[0031] The following further describes the specific embodiments of the present invention with reference to the accompanying drawings. It should be noted here that the description of these embodiments is for helping to understand the present invention, but does not constitute a limitation to the present invention.

[0032] In addition, the technical features involved in the various embodiments of the present invention described below can be combined with each other as long as they do not conflict with each other.

[0033] Please refer to the attached Figure 1 - attached Figure 10 In the wastewater treatment workshop of a large chemical enterprise, a large amount of production wastewater containing ammonia nitrogen is continuously generated every day. If these wastewaters are directly discharged without effective treatment, they will cause serious pollution to the surrounding environment. During the actual operation process, the wastewater first flows into the gas-liquid separation link. However, due to incomplete gas-liquid separation, liquids containing a high concentration of ammonia nitrogen often accidentally enter the subsequent treatment link for carbon-nitrogen wastewater. This not only greatly increases the treatment load of the ammonia nitrogen treatment mechanism, making the treatment equipment operate at a high load for a long time, but also significantly reduces the treatment efficiency and effect of ammonia nitrogen, resulting in the treated wastewater being difficult to meet the strict discharge standards.

[0034] In addition, the treatment device lacks an effective combination mechanism between the gas-liquid separation and the ammonia nitrogen stirring mechanism. When the gas-liquid separation device is in a highly efficient separation state, a large amount of separated ammonia nitrogen could have been treated in a timely manner, but at this time, the ammonia nitrogen stirring mechanism cannot respond and adjust the working parameters in a timely manner, and cannot make full use of the results of gas-liquid separation, thus causing serious waste of treatment resources. In this case, the enterprise not only has to bear higher treatment costs, but also is difficult to achieve precise, efficient, and energy-saving treatment of ammonia nitrogen wastewater, and cannot meet the increasingly strict environmental protection requirements and complex and changeable wastewater treatment conditions.

[0035] Therefore, a rapid treatment device for high-concentration ammonia-nitrogen wastewater of the present invention includes a device main body 1, a main box body 2, and a side box assembly 3. The side box assembly 3 includes a stirring box body A31 and a stirring box body B32, and the stirring box body A31 and the stirring box body B32 are respectively located on both sides of the main box body 2. The device main body 1 includes a heating assembly 5 for accelerating volatilization, a gas-liquid separation assembly 6 connected to the heating assembly 5, and a stirring assembly 8 connected to the gas-liquid separation assembly 6. The gas-liquid separation assembly 6 includes a motor 61 and a transmission box body one 62. A cyclone separator 63 is arranged on both motors 61 through a rotating shaft. The gas-liquid separation assembly 6 is arranged inside the transmission box body one 62. The staff processes carbon and nitrogen through the gas-liquid separation assembly 6 and the heating assembly 5, which is convenient for subsequent stirring operations. Taking the cyclone separator 63 as an example, the steam and ammonia-nitrogen mixed gas generated from the inner heating kettle 52 tangentially enters the cyclone separator 63. Under the action of centrifugal force, the liquid droplets and larger particles are thrown towards the inner wall of the main box body 2 and flow down along the wall surface, while the gas is discharged from the top of the cyclone separator 63, thus realizing preliminary gas-liquid separation. For the gravity settling separator, after the mixed gas enters the separation space, due to the reduction in flow velocity, the liquid droplets naturally settle to the bottom of the separator under the action of gravity, and the gas is discharged from the upper part;

[0036] The heating assembly 5 includes a jacket 51, an inner heating kettle 52, and a heating pipe 53. The inner heating kettle 52 is arranged inside the jacket 51. The inner heating kettle 52 is made of stainless steel, has corrosion resistance, and can withstand a certain temperature and pressure. Two motors 61 are respectively connected to a compressor 54. A condenser 55 is arranged on the compressor 54. An evaporator 57 and an expansion valve 56 are arranged in sequence from top to bottom on the left side of the condenser 55. The compressor 54, the condenser 55, the expansion valve 56, and the evaporator 57 are all connected through the heating pipe 53 to form a closed circulation system. Two such closed circulation systems are arranged, both distributed on both sides inside the heating assembly 5, which is convenient for heating and cooling the liquid entering the heating pipe 53. The stirring assembly 8 includes a stirring rod 81, stirring blades 82, and a transmission belt 83. A plurality of stirring blades 82 are arranged on the stirring rod 81. Both ends of the transmission belt 83 are arranged on the stirring rod 81 and the rotating shaft respectively. The number of the stirring assemblies 8 is set to two. By transmitting the two transmission belts 83 to the rotating shaft, it is convenient to synchronously drive the two stirring rods 81 arranged at the bottom, saving resources. And setting two stirring assemblies 8 is convenient to realize stirring on the basis of gas-liquid separation. When the gas-liquid separation device is running, the liquid can be stirred evenly and efficiently. On the one hand, it accelerates the mass exchange between gas and liquid, promotes the more rapid separation of gases such as ammonia from the liquid, and effectively improves the effect and speed of gas-liquid separation; on the other hand, through stirring, the ammonia-nitrogen in the liquid is more evenly distributed, creating good conditions for subsequent possible chemical reactions or treatment steps, and ensuring the coherence and high efficiency of the entire ammonia-nitrogen wastewater treatment process;

[0037] In addition, the two stirring components 8 cooperate with each other, can cover a larger treatment area, reduce the dead corners of stirring in the liquid, further improve the quality and effect of stirring, and thus help to achieve the rapid and efficient treatment of high-concentration ammonia-nitrogen wastewater.

[0038] Embodiment 1: During the heating process, since it is necessary to improve the heating efficiency, and a series of complex physical and chemical reactions will occur when high-concentration ammonia-nitrogen wastewater is heated, and the requirements for the stability and continuity of heating are relatively high. After long-term operation, a single heating component 5 may experience performance degradation, affecting the heating effect. Therefore, considering the stability, continuity of heating and the need to cope with complex reactions, two heating components 5 are provided and evenly distributed on both sides of the main box body 2. Two stirring components 8 are provided and are respectively located inside the stirring box body A31 and the stirring box body B32. The stirring box body A31, the stirring box body B32 and the main box body 2 penetrate each other, and a transmission box body two 9 is provided on the conveyor belt 83 and the stirring rod 81;

[0039] Specifically, the motor 61 provides power for the compressor 54 to drive the compressor 54 to operate. The compressor 54 compresses the low-temperature and low-pressure gaseous refrigerant coming out of the evaporator 57 into a high-temperature and high-pressure gaseous refrigerant. After the high-temperature and high-pressure gaseous refrigerant enters the condenser 55, it releases heat through heat exchange with the external low-temperature medium (such as air or water), and condenses into a high-pressure liquid refrigerant by itself. The position where the condenser 55 flows out is connected to the expansion valve 56. After the high-pressure liquid refrigerant passes through the expansion valve 56, the pressure and temperature drop sharply, becoming a low-temperature and low-pressure gas-liquid two-phase state. The low-temperature and low-pressure gas-liquid two-phase refrigerant enters the evaporator 57, absorbs the heat of the external low-temperature heat source (such as air or water) in the evaporator 57, the refrigerant vaporizes and becomes a low-temperature and low-pressure gaseous refrigerant. The position where the evaporator 57 flows out is then connected back to the inlet of the compressor 54, and the gaseous refrigerant is sucked into the compressor 54 again for compression. In this way, the cycle is repeated to complete the entire heat pump or refrigeration cycle operation.

[0040] Embodiment 2: During the heating and separation process, although the cyclone separator 63 will separate ammonia nitrogen, there may still be a small amount of ammonia nitrogen carried in the steam. If directly discharged, these ammonia nitrogen will enter the atmosphere or the subsequent water circulation system, causing environmental pollution. Therefore, it is necessary to set up a treatment component 11 to treat the steam to remove the ammonia nitrogen in it. A treatment component 11 is provided inside the main box body 2. The treatment component 11 includes a treatment box 111 and a liquid storage tank 112. The treatment box 111 is arranged at the inner top of the main box body 2, and the liquid storage tank 112 is arranged on the top surface of the main box body 2. The liquid storage tank 112 is provided with a liquid inlet, and the bottom of the liquid storage tank 112 is connected with a liquid collecting plate 113 through a pipeline. Several liquid outlet pipes 114 are arranged at the bottom of the liquid collecting plate 113. The pipeline, the liquid collecting plate 113 and the liquid outlet pipes 114 are all arranged inside the treatment box 111.

[0041] Specifically, by setting the processing component 11, the check valve two is opened to allow steam to enter from the intake pipe 10. The bottom of the liquid storage tank 112 sprays a washing liquid containing acidic substances (such as dilute sulfuric acid) through the liquid outlet pipe 114. The ammonia nitrogen reacts with the acidic substances to form ammonium salts, which are thus absorbed by the washing liquid. Finally, by opening the check valve three, it is discharged through the outlet 12 to achieve the purpose of removing ammonia nitrogen.

[0042] Embodiment 3: Outlet 12 is provided on both outer walls of the treatment tank 111. The outlet 12 penetrates through the outer walls of the treatment tank 111 and the main body 2. A check valve three is provided on the outlet 12. A circulation component 13 is provided at the back of the device main body 1. The circulation component 13 includes a circulation pipe 131. A water inlet pipe 4 is provided at the back of the internal heating kettle 52 and the jacket 51. The water inlet pipe 4 is interconnected with the heating pipe 53. One end of the circulation pipe 131 is connected to the main body 2, and the other end is connected to the water inlet pipe 4, and the circulation pipe 131 is interconnected with the water inlet pipe 4. A pressure sensor 133 and a micro pump two 132 are sequentially arranged on the circulation pipe 131 from top to bottom;

[0043] Specifically, through the provided circulation component 13, when the concentration sensor detects that after the high-concentration ammonia nitrogen wastewater in the main body 2 has undergone preliminary treatment, the ammonia nitrogen concentration still fails to meet the expected discharge standard or subsequent treatment requirements, the concentration sensor will transmit the detection signal to the controller. After receiving the signal, the controller will automatically start the circulation component 13. At this time, the micro pump two 132 starts to work. Under its driving force, the liquid in the main body 2 is pumped to the water inlet pipe 4 through the circulation pipe 131, and then flows back into the area between the internal heating kettle 52 and the jacket 51 again;

[0044] During this process, the pressure sensor 133 will monitor the pressure condition in the circulation pipe 131 in real time and feedback the pressure data to the controller. Once the pressure shows abnormal fluctuations, the controller will timely adjust the working power of the micro pump two 132 to ensure the stable progress of the circulation process;

[0045] The wastewater that re-enters the area between the internal heating kettle 52 and the jacket 51 will undergo heating, separation, and stirring operations again. After being treated again, the wastewater will flow back into the main body 2 and wait for the concentration sensor to detect again. This cycle repeats until the concentration sensor detects that the ammonia nitrogen concentration reaches the expected target, and then the controller will stop the operation of the circulation component 13, thereby realizing the precise and efficient treatment of high-concentration ammonia nitrogen wastewater. The function of the expansion valve 56 is to sharply reduce the pressure of the liquid refrigerant, and at the same time, the temperature also drops accordingly, becoming a low-temperature and low-pressure liquid.

[0046] In the fourth embodiment, a micro pump I is provided on the water inlet pipe 4. Discharge pipes 14 are provided on both sides of the stirring tank body A31 and the stirring tank body B32. A connecting pipe 7 is provided at the bottom of the jacket 51 and the internal heating kettle 52. A check valve I is provided on the connecting pipe 7. An air inlet pipe 10 is provided between the treatment tank 111 and the jacket 51. A check valve II is provided on the air inlet pipe 10. A temperature sensor is provided inside the internal heating kettle 52, and a concentration sensor is provided inside the main box body 2. A controller is provided in front of the device main body 1. The controller is electrically connected to the pressure sensor 133, the temperature sensor, the concentration sensor, the motor 61, the micro pump I, and the micro pump II 132 respectively.

[0047] Specifically, by setting the concentration sensor, real-time concentration data reference is provided for the operator, which is convenient for grasping the progress and effect of wastewater treatment at any time. The operator can flexibly adjust various parameters of the treatment device, such as heating temperature, reaction time, etc., according to the information fed back by the concentration sensor, to ensure the efficient and stable operation of the entire treatment process, so as to achieve the precise and rapid treatment of high-concentration ammonia-nitrogen wastewater and effectively improve the working efficiency and treatment quality of the treatment device.

[0048] Specifically, the controller is built-in with a PID control module, which receives the signals of the pressure sensor 133, the temperature sensor, the concentration sensor, the motor 61, the micro pump I, and the micro pump II 132 in real time. By setting the pressure sensor 133 to be electrically connected to the controller, it is convenient to detect and control the pressure condition of the circulation pipe 131 in real time, and timely adjust the power of the micro pump II 132 to maintain the stable progress of the circulation.

[0049] Working principle:

[0050] First, when using the device main body 1 to filter ammonia-nitrogen wastewater, first the raw material enters the heating tube 53 in the heating assembly 5 through the water inlet pipe 4. The compressor 54 starts first. It compresses the low-temperature and low-pressure gaseous refrigerant, making it into a high-temperature and high-pressure gas and entering the condenser 55. The refrigerant exchanges heat with the external environment or the cooling medium (such as water or air), and the released heat is effectively transferred to the heating tube 53 to heat the wastewater. It is throttled and depressurized through the expansion valve 56. Finally, the low-temperature and low-pressure liquid refrigerant enters the evaporator 57. The refrigerant absorbs the heat in the ammonia-nitrogen wastewater treatment system, vaporizes, and turns back into a low-temperature and low-pressure gas, and then is sucked into the compressor 54 again to complete the entire heat pump or refrigeration cycle operation. The check valve II is opened, and finally the steam enters the inside of the treatment tank 111 in the treatment assembly 11. The washing liquid containing acidic substances (such as dilute sulfuric acid) is sprayed through the liquid outlet pipe 114. The ammonia-nitrogen reacts with the acidic substances to form ammonium salts, which are thus absorbed by the washing liquid. Finally, by opening the check valve III, it is discharged through the outlet 12. The temperature sensor senses the temperature inside the internal heating kettle 52 in real time;

[0051] Meanwhile, under the action of the motor 61, the two cyclone separators 63 and the two stirring rods 81 at the bottom rotate synchronously. Eventually, the ammonia nitrogen particles enter the interiors of the main box body 2, the stirring box body A31, and the stirring box body B32. With the cooperation of the gas-liquid separation component 6 and the stirring component 8, the concentration sensor detects the particles in the main box body 2 in real time. The two stirring rods 81 stir the ammonia nitrogen particles, effectively preventing the ammonia nitrogen particles from solidifying. Then, the ammonia nitrogen particles are conveyed into the discharge pipe 14, and the discharge pipe 14 discharges the ammonia nitrogen particles from the two discharge ports respectively. If the concentration sensor detects that the concentration of the ammonia nitrogen particles in the main box body 2 does not reach the standard preset by the expected controller, the concentration sensor immediately transmits the detection signal to the controller, and restarts the micro pump two 132 in the circulation component 13 to enter the water inlet pipe 4 for processing again. The pressure sensor 133 monitors the pressure in the circulation pipe 131 in real time, and after re-heating through the internal heating kettle 52 and the jacket 51, separation by the gas-liquid separation component 6, and stirring by the stirring component 8 and other processes, until the concentration of the ammonia nitrogen particles in the main box body 2 reaches the expected standard. Thus, the entire working process ends.

[0052] The above front, back, left, right, up, and down are all based on the Figure 1 description in the attached drawings of the specification.

[0053] In the description of the present invention, it should be understood that the orientation or positional relationships indicated by the terms "center", "longitudinal", "transverse", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc. are based on the orientation or positional relationships shown in the attached drawings, and are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore should not be construed as limiting the protection scope of the present invention.

[0054] The above has described the embodiments of the present invention in detail with reference to the attached drawings, but the present invention is not limited to the described embodiments.

[0055] For those skilled in the art, without departing from the principles and spirit of the present invention, various changes, modifications, substitutions, and variations made to these embodiments still fall within the protection scope of the present invention.

Claims

1. A rapid treatment device for high-concentration ammonia-nitrogen wastewater, comprising a device main body (1), a main box body (2) and a side box assembly (3). The side box assembly (3) includes a stirring box body A (31) and a stirring box body B (32). The stirring box body A (31) and the stirring box body B (32) are respectively located on both sides of the main box body (2), and it is characterized in that: The device main body (1) includes a heating component (5) for accelerating volatilization, a gas-liquid separation component (6) connected to the heating component (5), and a stirring component (8) connected to the gas-liquid separation component (6). The gas-liquid separation component (6) includes a motor (61) and a first transmission box body (62). A cyclone separator (63) is arranged on each of the two motors (61) through a rotating shaft. The gas-liquid separation component (6) is arranged inside the first transmission box body (62). The heating component (5) includes a jacket (51), an internal heating kettle (52), and a heating pipe (53). The internal heating kettle (52) is arranged inside the jacket (51). Each of the two motors (61) is connected to a compressor (54). A condenser (55) is arranged on the compressor (54). An evaporator (57) and an expansion valve (56) are arranged in sequence from top to bottom on the left side of the condenser (55). The compressor (54), the condenser (55), the expansion valve (56), and the evaporator (57) are all connected through the heating pipe (53) to form a closed circulation system. The stirring component (8) includes a stirring rod (81), stirring blades (82), and a conveyor belt (83). A plurality of the stirring blades (82) are arranged on the stirring rod (81). Both ends of the conveyor belt (83) are respectively arranged on the stirring rod (81) and the rotating shaft.

2. The rapid treatment device for high-concentration ammonia-nitrogen wastewater according to claim 1, wherein: Two heating components (5) are provided and are evenly distributed on both sides of the main box body (2). Two stirring components (8) are provided and are respectively located inside a stirring box body A (31) and a stirring box body B (32). The stirring box body A (31), the stirring box body B (32), and the main box body (2) penetrate through each other. A second transmission box body (9) is arranged on the conveyor belt (83) and the stirring rod (81).

3. The rapid treatment device for high-concentration ammonia-nitrogen wastewater according to claim 2, wherein: A processing component (11) is arranged inside the main box body (2). The processing component (11) includes a processing box (111) and a liquid storage tank (112). The processing box (111) is arranged at the inner top of the main box body (2). The liquid storage tank (112) is arranged on the top surface of the main box body (2). A liquid inlet is arranged on the liquid storage tank (112). The bottom of the liquid storage tank (112) is connected to a liquid collecting plate (113) through a pipeline. A plurality of liquid outlet pipes (114) are arranged at the bottom of the liquid collecting plate (113). The pipeline, the liquid collecting plate (113), and the liquid outlet pipes (114) are all arranged inside the processing box (111).

4. The rapid treatment device for high-concentration ammonia nitrogen wastewater according to claim 3, characterized in that: Exits (12) are opened on both outer walls of the processing box (111). The exits (12) penetrate through the outer walls of the processing box (111) and the main box body (2). Check valves III are arranged on the exits (12).

5. The rapid treatment device for high-concentration ammonia-nitrogen wastewater according to claim 4, wherein: A circulation component (13) is provided at the rear of the device main body (1). The circulation component (13) includes a circulation pipe (131). A water inlet pipe (4) is provided at the rear of the inner heating kettle (52) and the jacket (51). The water inlet pipe (4) is in communication with a heating pipe (53). One end of the circulation pipe (131) is connected to the main box body (2), and the other end is connected to the water inlet pipe (4), and the circulation pipe (131) is in communication with the water inlet pipe (4). A pressure sensor (133) and a micro pump two (132) are sequentially arranged on the circulation pipe (131) from top to bottom.

6. The rapid treatment device for high-concentration ammonia nitrogen wastewater according to claim 5, wherein: A micro pump one is provided on the water inlet pipe (4). Discharge pipes (14) are provided on both sides of the stirring box body A (31) and the stirring box body B (32).

7. A rapid treatment device for high-concentration ammonia nitrogen wastewater according to claim 5, characterized in that: A connecting pipe (7) is provided at the bottom of the jacket (51) and the inner heating kettle (52). A check valve one is provided on the connecting pipe (7).

8. A rapid treatment device for high-concentration ammonia-nitrogen wastewater according to claim 4, characterized in that: An air inlet pipe (10) is provided between the treatment box (111) and the jacket (51). A check valve two is provided on the air inlet pipe (10).

9. The rapid treatment device for high-concentration ammonia-nitrogen wastewater according to claim 7, wherein: A temperature sensor is provided inside the inner heating kettle (52). A concentration sensor is provided inside the main box body (2). A controller is provided in front of the device main body (1). The controller is electrically connected to the pressure sensor (133), the temperature sensor, the concentration sensor, the motor (61), the micro pump one, and the micro pump two (132) respectively.

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