Industrial wastewater treatment equipment with exhaust gas purification function

Abstract

The application discloses an industrial wastewater treatment equipment with waste gas purification function, relates to the technical field of wastewater treatment, and is used for treating impurities in wastewater. The treatment equipment comprises a main body mechanism, an impurity separation mechanism, an impurity detection mechanism, a solution separation mechanism and a waste gas filtering mechanism. The main body mechanism is connected with the impurity separation mechanism, the main body mechanism is connected with the impurity detection mechanism, the main body mechanism is connected with the solution separation mechanism, the main body mechanism is connected with the waste gas filtering mechanism, the impurity separation mechanism is connected with the solution separation mechanism, the main body mechanism comprises a mounting base and a reaction device, the reaction device is arranged on the mounting base, the reaction device comprises a reaction tank and a heating resistance wire, the reaction tank is tightly connected with the mounting base, the heating resistance wire is arranged in the tank wall of the reaction tank, the heating resistance wire is connected with a power supply, and the mounting base is connected with the impurity separation mechanism.

Description

Technical Field

[0001] This invention relates to the field of wastewater treatment technology, specifically to an industrial wastewater treatment device with an additional waste gas purification function. Background Technology

[0002] Wastewater treatment is an indispensable part of industrial production. Industrial wastewater treatment technologies are developing in a diversified manner, mainly including physical, chemical, and biological methods. Physical methods include sedimentation, filtration, centrifugation, flotation, evaporation crystallization, and reverse osmosis, which are mainly used to remove suspended solids, colloids, and oily substances from wastewater.

[0003] Current wastewater treatment methods mostly employ sedimentation filtration and flotation to separate colloids and flocs. These methods are largely mechanical and have low efficiency. Furthermore, while flotation is commonly used for flocs, the size of the flocs cannot be standardized or determined. The amount of gas produced by flotation is also uniform, which may prevent the gas from supporting larger flocs. For the removal of colloids, natural sedimentation is slow, which affects treatment efficiency. In addition, most methods complete the treatment within a limited time, which cannot guarantee the separation of internal water and impurities. Summary of the Invention

[0004] The purpose of this invention is to provide an industrial wastewater treatment device with an auxiliary exhaust gas purification function to solve the problems raised in the prior art.

[0005] To achieve the above objectives, the present invention provides the following technical solution:

[0006] The treatment equipment is used to treat impurities in wastewater. The treatment equipment includes a main body, an impurity separation mechanism, an impurity detection mechanism, a solution separation mechanism, and an exhaust gas filtration mechanism. The main body is connected to the impurity separation mechanism, the impurity detection mechanism, the solution separation mechanism, and the exhaust gas filtration mechanism. The impurity separation mechanism is also connected to the solution separation mechanism.

[0007] In this treatment equipment, the equipment is used to filter out impurities from wastewater. The main body provides the treatment site, the impurity separation mechanism is used to separate colloids and flocculents from water in the wastewater, the impurity detection mechanism is used to detect the impurity content in the wastewater in real time, the solution separation mechanism is used to discharge the separated impurities and water, and the exhaust gas filtration mechanism is used to remove the exhaust gas carried during the transportation of wastewater and to perform initial purification.

[0008] Furthermore, the main structure includes a mounting base and a reaction device. The reaction device is placed on the mounting base and includes a reaction vessel and a heating resistance wire. The reaction vessel and the mounting base are fastened together. The heating resistance wire is placed inside the wall of the reaction vessel and is connected to a power source. The mounting base is connected to an impurity separation mechanism, an exhaust gas filtration mechanism, an impurity separation mechanism, an impurity detection mechanism, a solution separation mechanism, a reaction vessel, an impurity separation mechanism, an impurity detection mechanism, and a solution separation mechanism.

[0009] In the main structure, the mounting base is used to provide a supporting foundation for wastewater treatment. The wastewater enters the reaction device to react and the impurities are separated in the reaction tank. At the same time, heating resistance wires are wound inside the reaction tank wall. During the process of impurity separation in the wastewater, the heating resistance wires are energized to heat the wastewater in the reaction tank, making the impurity separation more efficient.

[0010] Furthermore, the impurity separation mechanism includes a colloid separation device connected to a reaction vessel. The colloid separation device includes a metal electrode and a first energized wire. The metal electrode is placed inside the reaction vessel, with one end of the metal electrode extending out of the vessel near the bottom wall. The extended end of the metal electrode is connected to the first energized wire. The colloid separation device also includes an auxiliary separation device connected to a mounting base and the reaction vessel. The auxiliary separation device includes a drive motor, a drive rod, and drive blades. The fixed end of the drive motor is securely connected to the mounting base, and the output end of the drive motor is rotatably connected to the bottom of the reaction vessel. The drive rod is placed inside the reaction vessel, with one end of the drive rod securely connected to the output end of the drive motor and the other end of the drive rod rotatably connected to the top of the reaction vessel. Several drive blades are placed inside the reaction vessel, and these drive blades are securely connected to the drive rod, positioned at the lower third of the drive rod. The colloid separation device is connected to a solution separation mechanism, the auxiliary separation device is connected to the solution separation mechanism, and the drive rod is connected to the solution separation mechanism.

[0011] In the impurity separation mechanism, colloids in wastewater are separated by a colloid separation device. The separation of colloids and water is achieved through metal electrodes. Under the action of an external voltage, the metal electrodes generate a large number of cations, which agglomerate colloidal pollutants to achieve the separation of pollutants. In this process, cations adsorb colloids, forming particles that settle to the bottom, thus achieving the separation of colloids and water. At the same time, an auxiliary separation device assists in the separation of colloids and water. A drive motor drives a drive rod to rotate, which in turn drives a drive fan blade to rotate, thereby carrying the particles formed by cations and colloids to collide with the reaction tank wall. After losing force, they fall more quickly, thereby improving the impurity separation efficiency.

[0012] Furthermore, the impurity separation mechanism also includes a floc separation device, which is connected to the reaction tank. The floc separation device includes an insoluble electrode and a second energized wire. The insoluble electrode is placed in the reaction tank, with one end of the insoluble electrode near the bottom wall of the reaction tank extending out of the tank. The extended end of the insoluble electrode is connected to the second energized wire. The floc separation device also includes a spreading device, which is connected to the reaction tank and the insoluble electrode. The spreading device includes a secondary electrode and a telescopic rod. The secondary electrode and the insoluble electrode overlap and are rotatably connected by a rotating rod. The secondary electrode and the telescopic rod are fastened together, with the end of the telescopic rod away from the secondary electrode fastened to the wall of the reaction tank.

[0013] In the impurity separation mechanism, floc separation devices separate flocs in wastewater. During the separation of colloids, hydrogen microbubbles are generated on the cathode of the metal electrode under the action of an external voltage. These microbubbles adhere to the flocs and float upwards. At the same time, the cathode of the insoluble electrode also generates a large amount of hydrogen under the action of an external voltage. The two work together to produce more hydrogen. As the hydrogen rises, it can lift the flocs, thus achieving the separation of flocs and water. In the early separation stage, the electrolysis area is increased by the unfolding device, resulting in more hydrogen molecules being generated. The telescopic rod pushes the secondary electrode to rotate along the rotating rod, forming a certain angle between the secondary electrode and the insoluble electrode, thereby increasing the electrolysis area and improving the impurity separation efficiency. In the later stage, when there are fewer impurities, the telescopic rod can be retracted, reducing the electrolysis area and minimizing useless electrolysis.

[0014] Furthermore, the impurity detection mechanism includes a detection box, a detection light source, and a photoresistor. The impurity detection mechanism is placed in the reaction vessel, and the detection box is firmly connected to the wall of the reaction vessel. The detection box is located in the middle of the reaction vessel. The detection light source is firmly connected to the detection box. Several photoresistors are provided, and the several photoresistors are closely attached to each other. The photoresistors are firmly connected to the inner wall of the reaction vessel. The connection between the middle photoresistor and the middle of the detection box is on one diameter of the reaction vessel.

[0015] In the impurity detection mechanism, this device is located in the middle of the reaction tank to detect the wastewater inside. Since flocs and colloids rise and sink respectively under the influence of hydrogen molecules and cations, only the water in the middle section needs to be detected. Detection is performed using a detection light source and a photoresistor. The wall of the detection box facing the light source is transparent. For light-transmitting colloids, the light from the detection light source will be refracted, shining on different positions of the photoresistor. However, for opaque colloids and flocs, they can directly block the light from the detection light source, reducing the amount of light falling on the photoresistor. At this time, the resistance of the photoresistor decreases. At this time, the telescopic rod remains extended, continuously electrolyzing more hydrogen to help the flocs rise. Simultaneously, for larger flocs, it can block more light sources. By increasing the electrolysis area through the telescopic rod, more hydrogen can be generated, supporting the larger flocs. Meanwhile, the auxiliary separation device continues to operate, assisting the colloids to settle. When more light shines on the photoresistor and less refraction occurs, it indicates fewer impurities and a higher photoresistor resistance. The telescopic rod can then retract to its original position, allowing the insoluble electrode and secondary electrode to overlap again, reducing the electrolysis area. The auxiliary separation device appropriately reduces its rotation speed to assist the colloids to settle.

[0016] Furthermore, the solution separation mechanism includes an inlet pipe, a first outlet pipe, a second outlet pipe, and a third outlet pipe. The inlet pipe is connected to the top of the reaction tank, and the first, second, and third outlet pipes are connected to the upper, middle, and lower side walls of the reaction tank, respectively. The inlet pipe is connected to the exhaust gas filtration mechanism.

[0017] In the solution separation mechanism, wastewater is injected into the reaction tank through the inlet pipe. After the impurities are separated, that is, when hydrogen lifts the flocs to the top, the cation adsorbed colloids sink to the bottom, and the wastewater with very few impurities is in the middle, the corresponding clean solution and impurity solution are discharged through the first outlet pipe, the second outlet pipe, and the third outlet pipe, respectively.

[0018] Furthermore, the exhaust gas filtration mechanism includes an air guide pipe, a semi-permeable membrane, and a filter chamber. The air guide pipe is connected to the liquid inlet pipe, and a semi-permeable membrane is provided between the air guide pipe and the liquid inlet pipe. The semi-permeable membrane allows gas to pass through. The filter chamber is placed on the mounting base, and the end of the air guide pipe away from the liquid inlet pipe is connected to the filter chamber. Activated carbon is provided in the filter chamber.

[0019] In the exhaust gas filtration system, as the waste liquid enters the reaction tank through the inlet pipe, it may carry some waste gas. The waste gas is collected by a side-opening gas guide pipe and screened through a semi-permeable membrane. The semi-permeable membrane only allows gas to pass through. The waste gas passes through the semi-permeable membrane and enters the filtration chamber along the gas guide pipe. It is then preliminarily purified by the activated carbon inside before being discharged for further purification.

[0020] Compared with the prior art, the beneficial effects of the present invention are as follows: By setting a heating resistance wire, the internal wastewater temperature is increased during device operation, thereby improving impurity separation efficiency. An impurity separation mechanism separates colloids, flocs, and water in the wastewater. The separation of colloids and water is achieved through a metal electrode. Under external voltage, the metal electrode generates a large number of cations, which adsorb the colloids, forming particles that settle to the bottom, thus achieving separation of colloids and water. An auxiliary separation device assists in the separation by driving a fan blade to rotate, carrying cations and adsorbed colloid particles that collide with the reaction tank wall. After losing force, the particles fall more quickly, further improving impurity separation efficiency. Under external voltage, the cathode of the metal electrode and the insoluble electrode generates a large amount of hydrogen gas. The combined effect of these two components produces a significant amount of hydrogen gas, which floats the flocs, thus separating the flocs and water. A telescopic rod drives the auxiliary electrode to rotate, increasing the electrolysis area and improving impurity separation efficiency. An impurity detection mechanism enables real-time detection of impurities, and adjustments are made to the impurity separation mechanism based on the detection results, achieving highly efficient impurity separation. Attached Figure Description

[0021] Figure 1 This is a schematic diagram of the overall structure of the present invention;

[0022] Figure 2 This is a top view of the present invention;

[0023] Figure 3 for Figure 2 AA section view;

[0024] Figure 4 for Figure 2 BB section view;

[0025] Figure 5 for Figure 2 CC section view;

[0026] Figure 6 for Figure 5 Partial D magnified view;

[0027] Figure 7 This is a schematic diagram of the interior of the reaction vessel;

[0028] Figure 8 This is a schematic diagram of the activation of the unfolding device of the present invention.

[0029] In the diagram: 1. Main structure; 11. Mounting base; 12. Reaction device; 121. Reaction vessel; 122. Heating resistance wire; 2. Impurity separation mechanism; 21. Colloidal separation device; 211. Metal electrode; 212. Auxiliary separation device; 2121. Drive motor; 2122. Drive rotor; 2123. Drive fan blade; 22. Floc separation device; 221. Insoluble electrode; 222. Unfolding device; 2221. Secondary electrode; 2222. Telescopic rod; 3. Impurity detection mechanism; 31. Detection box; 32. Detection light source; 33. Photoresistor; 4. Solution separation mechanism; 41. Inlet pipe; 42. First outlet pipe; 43. Second outlet pipe; 44. Third outlet pipe; 5. Waste gas filtration mechanism; 51. Air guide pipe; 52. Semi-permeable membrane; 53. Filtration chamber. Detailed Implementation

[0030] 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.

[0031] Example: Figures 1-8 As shown, the present invention provides a technical solution for an industrial wastewater treatment device with an additional exhaust gas purification function. The treatment device is used to treat impurities in wastewater. The treatment device includes a main body 1, an impurity separation mechanism 2, an impurity detection mechanism 3, a solution separation mechanism 4, and an exhaust gas filtration mechanism 5. The main body 1 is connected to the impurity separation mechanism 2, the main body 1 is connected to the impurity detection mechanism 3, the main body 1 is connected to the solution separation mechanism 4, the main body 1 is connected to the exhaust gas filtration mechanism 5, and the impurity separation mechanism 2 is connected to the solution separation mechanism 4.

[0032] In this treatment equipment, the equipment is used to filter out impurities from wastewater. The main body 1 provides the treatment site, the impurity separation unit 2 is used to separate colloids and flocculents from water in the wastewater, the impurity detection unit 3 is used to detect the impurity content in the wastewater in real time, the solution separation unit 4 is used to discharge the separated impurities and water, and the exhaust gas filtration unit 5 is used to remove the exhaust gas carried during the transportation of wastewater and to perform initial purification.

[0033] The main structure 1 includes a mounting base 11 and a reaction device 12. The reaction device 12 is placed on the mounting base 11 and includes a reaction vessel 121 and a heating resistance wire 122. The reaction vessel 121 and the mounting base 11 are fastened together. The heating resistance wire 122 is placed inside the wall of the reaction vessel 121 and is connected to a power source. The mounting base 11 is connected to the impurity separation mechanism 2 and the exhaust gas filtration mechanism 5. The reaction device 12 is connected to the impurity separation mechanism 2, the impurity detection mechanism 3, and the solution separation mechanism 4. The reaction vessel 121 is connected to the impurity separation mechanism 2, the impurity detection mechanism 3, and the solution separation mechanism 4.

[0034] In the main structure 1, the mounting base 11 is used to provide a supporting foundation for wastewater treatment. The wastewater will enter the reaction device 12 for reaction, and the separation of impurities will be completed in the reaction tank 121. At the same time, a heating resistance wire 122 is wound inside the wall of the reaction tank 121. During the process of impurity separation of wastewater, the heating resistance wire 122 is energized to heat the wastewater in the reaction tank 121, making the impurity separation efficiency higher.

[0035] The impurity separation mechanism 2 includes a colloidal separation device 21 connected to a reaction vessel 121. The colloidal separation device 21 includes a metal electrode 211 and a first energizing wire. The metal electrode 211 is placed inside the reaction vessel 121, with one end of the metal electrode 211 extending out of the vessel near the bottom wall. This extended end of the metal electrode 211 is connected to the first energizing wire. The colloidal separation device 21 also includes an auxiliary separation device 212 connected to a mounting base 11 and the reaction vessel 121. The auxiliary separation device 212 includes a drive motor 2121, a drive rotor 2122, and a drive fan blade 2123. The fixed end of the drive motor 2121 is connected to the mounting base 11. The drive motor 2121 is rotatably connected to the bottom of the reaction vessel 121. The drive rod 2122 is placed inside the reaction vessel 121. One end of the drive rod 2122 is rotatably connected to the output end of the drive motor 2121, and the other end of the drive rod 2122 is rotatably connected to the top of the reaction vessel 121. The drive fan blades 2123 are placed inside the reaction vessel 121. There are several drive fan blades 2123. Several drive fan blades 2123 are rotatably connected to the drive rod 2122. The drive fan blades 2123 are placed at the lower third of the drive rod 2122. The colloid separation device 21 is connected to the solution separation mechanism 4. The auxiliary separation device 212 is connected to the solution separation mechanism 4. The drive rod 2122 is connected to the solution separation mechanism 4.

[0036] In the impurity separation mechanism 2, colloids in the wastewater are separated by a colloid separation device 21. The separation of colloids and water is achieved by a metal electrode 211. Under the action of an external voltage, the metal electrode 211 generates a large number of cations, which coagulate the colloidal pollutants to achieve the separation of pollutants. In this process, the cations adsorb the colloids, form particles, and then settle to the bottom, thus achieving the separation of colloids and water. At the same time, the separation of colloids and water is assisted by an auxiliary separation device 212. The drive motor 2121 drives the drive rod 2122 to rotate the drive fan blade 2123, thereby carrying the particles formed by cations and colloids to collide with the wall of the reaction tank 121. After losing force, they fall more quickly, thereby improving the impurity separation efficiency.

[0037] The impurity separation mechanism 2 also includes a floc separation device 22, which is connected to the reaction tank 121. The floc separation device 22 includes an insoluble electrode 221 and a second energizing wire. The insoluble electrode 221 is placed in the reaction tank 121, with one end of the insoluble electrode 221 near the bottom wall of the reaction tank 121 extending out of the tank. The extended end of the insoluble electrode 221 is connected to the second energizing wire. The floc separation device 22 also includes a unfolding device 222, which is connected to the reaction tank 121 and the insoluble electrode 221. The unfolding device 222 includes a secondary electrode 2221 and a telescopic rod 2222. The secondary electrode 2221 and the insoluble electrode 221 overlap and are rotatably connected by a rotating rod. The secondary electrode 2221 and the telescopic rod 2222 are tightly connected, with the end of the telescopic rod 2222 away from the secondary electrode 2221 being tightly connected to the wall of the reaction tank 121.

[0038] In the impurity separation mechanism 2, flocs in the wastewater are separated by the floc separation device 22. During the separation of colloids, hydrogen microbubbles are generated on the cathode of the metal electrode 211 under the action of external voltage. These microbubbles adhere to the flocs and float upwards. At the same time, the cathode of the insoluble electrode 221 also generates a large amount of hydrogen under the action of external voltage. The two work together to produce more hydrogen. During the process of hydrogen floating, it can float the flocs, thereby achieving the separation of flocs and water. In the early separation, the electrolysis area is increased by the unfolding device 222, resulting in more hydrogen molecules being generated. The telescopic rod 2222 pushes the auxiliary electrode 2221 to rotate along the rotating rod, so that the auxiliary electrode 2221 and the insoluble electrode 221 form a certain angle, thereby increasing the electrolysis area and improving the impurity separation efficiency. In the later stage, when there are fewer impurities, the telescopic rod 2222 can be retracted, reducing the electrolysis area and reducing useless electrolysis.

[0039] The impurity detection mechanism 3 includes a detection box 31, a detection light source 32, and a photoresistor 33. The impurity detection mechanism 3 is placed in the reaction vessel 121. The detection box 31 is tightly connected to the wall of the reaction vessel 121 and is located in the middle of the reaction vessel 121. The detection light source 32 is tightly connected to the detection box 31. Several photoresistors 33 are provided and are tightly attached to each other. The photoresistors 33 are tightly connected to the inner wall of the reaction vessel 121. The connecting line between the middle photoresistor 33 and the detection box 31 is on a diameter of the reaction vessel 121.

[0040] In the impurity detection mechanism 3, this mechanism is located in the middle of the reaction tank 121 to detect the wastewater inside. Since flocs and colloids rise and sink respectively under the action of hydrogen molecules and cations, only the water in the middle section needs to be detected. Detection is performed using a detection light source 32 and a photoresistor 33. The wall of the detection box 31 facing the light source is transparent. For light-transmitting colloids, the light from the detection light source 32 will be refracted and shine on different positions of the photoresistor 33. However, for opaque colloids and flocs, they can directly block the light from the detection light source 32, reducing the amount of light falling on the photoresistor 33. At this time, the resistance of the photoresistor 33 decreases, and the telescopic rod... 2222 remains extended, continuously electrolyzing more hydrogen to help the flocs rise. At the same time, for larger flocs, it can block more light sources. By increasing the electrolysis area through the telescopic rod 2222, more hydrogen can be generated to support the larger flocs. Meanwhile, the auxiliary separation device 212 is also continuously activated to assist the colloids in settling. When the detection light source 32 shines more on the photoresistor 33 and there is less refraction, it indicates that there are fewer impurities. The resistance of the photoresistor 33 is relatively high, and the telescopic rod 2222 can retract to its original position. The insoluble electrode 221 and the secondary electrode 2221 overlap again, reducing the electrolysis area. The auxiliary separation device 212 appropriately reduces its rotation speed to assist the colloids in settling.

[0041] The solution separation mechanism 4 includes an inlet pipe 41, a first outlet pipe 42, a second outlet pipe 43, and a third outlet pipe 44. The inlet pipe 41 is connected to the top of the reaction tank 121. The first outlet pipe 42, the second outlet pipe 43, and the third outlet pipe 44 are respectively connected to the upper, middle, and lower side walls of the reaction tank 121. The inlet pipe 41 is connected to the exhaust gas filtration mechanism 5.

[0042] In the solution separation mechanism 4, wastewater is injected into the reaction tank 121 through the inlet pipe 41. After the impurity separation is completed, that is, when hydrogen lifts the flocs to the top, the cation adsorbed colloids sink to the bottom, and the wastewater with very few impurities is in the middle, the corresponding clean solution and impurity solution are discharged through the first outlet pipe 42, the second outlet pipe 43 and the third outlet pipe 44 respectively.

[0043] The exhaust gas filtration mechanism 5 includes an air guide pipe 51, a semi-permeable membrane 52, and a filter chamber 53. The air guide pipe 51 is connected to the liquid inlet pipe 41. A semi-permeable membrane 52 is provided between the air guide pipe 51 and the liquid inlet pipe 41. The semi-permeable membrane 52 allows gas to pass through. The filter chamber 53 is placed on the mounting base 11. The end of the air guide pipe 51 away from the liquid inlet pipe 41 is connected to the filter chamber 53. Activated carbon is provided inside the filter chamber 53.

[0044] In the exhaust gas filtration mechanism 5, during the process of the waste liquid entering the reaction tank 121 through the inlet pipe 41, it may carry some waste gas. The waste gas is collected by connecting a side-opening gas guide pipe 51 and screened through a semi-permeable membrane 52. The semi-permeable membrane 52 can only allow gas to pass through. The waste gas passes through the semi-permeable membrane 52 and enters the filter chamber 53 along the gas guide pipe 51. It is then preliminarily purified by the activated carbon inside and then discharged for other purification operations.

[0045] Working principle of this invention: This invention utilizes a heating resistance wire 122 to raise the internal wastewater temperature during operation, improving impurity separation efficiency. An impurity separation mechanism 2 separates colloids, flocs, and water from the wastewater. The separation of colloids and water is achieved through a metal electrode 211. Under external voltage, the metal electrode 211 generates a large number of cations, which adsorb the colloids, forming particles that settle to the bottom, thus separating the colloids and water. An auxiliary separation device 212 assists in the separation, driving the fan blades 2123 to rotate, carrying the cations and adsorbed colloids... The particles collide with the wall of the reaction vessel 121 and fall more quickly after losing force, thereby improving the impurity separation efficiency. Under the action of an external voltage, the cathode of the metal electrode 211 and the insoluble electrode 221 generates a large amount of hydrogen gas. The two work together to produce more hydrogen gas. During the process of hydrogen gas rising, it can float the flocs, thereby achieving the separation of flocs and water. The auxiliary electrode 2221 is driven to rotate by the telescopic rod 2222, which increases the electrolysis area and improves the impurity separation efficiency. By setting an impurity detection mechanism 3, the impurities can be detected in real time. At the same time, the impurity separation mechanism 2 is adjusted according to the detection, thereby achieving efficient impurity separation.

[0046] It will be apparent to those skilled in the art that the present invention is not limited to the details of the exemplary embodiments described above, and that the invention can be implemented in other specific forms without departing from its spirit or essential characteristics. Therefore, the embodiments should be considered in all respects as exemplary and non-limiting, and the scope of the invention is defined by the appended claims rather than the foregoing description. Thus, all variations falling within the meaning and scope of equivalents of the claims are intended to be included within the present invention. No reference numerals in the claims should be construed as limiting the scope of the claims.

Claims

1. An industrial wastewater treatment device with an attached exhaust gas purification function, the device being used to treat impurities in wastewater, characterized in that: The processing equipment includes a main body (1), an impurity separation mechanism (2), an impurity detection mechanism (3), a solution separation mechanism (4), and a waste gas filtration mechanism (5). The main body (1) and the impurity separation mechanism (2) are connected, the main body (1) and the impurity detection mechanism (3) are connected, the main body (1) and the solution separation mechanism (4) are connected, the main body (1) and the waste gas filtration mechanism (5) are connected, and the impurity separation mechanism (2) and the solution separation mechanism (4) are connected. The main body (1) includes a mounting base (11) and a reaction device (12). The reaction device (12) is placed on the mounting base (11). The reaction device (12) includes a reaction vessel (121) and a heating resistance wire (122). The reaction vessel (121) and the mounting base (11) are fastened together. The heating resistance wire (122) is placed inside the wall of the reaction vessel (121). The heating resistance wire (122) is connected to a power source. The impurity separation mechanism (2) includes a colloidal separation device (21), which is connected to the reaction vessel (121). The colloidal separation device (21) includes a metal electrode (211) and a first energized wire. The metal electrode (211) is placed inside the reaction vessel (121). One end of the metal electrode (211) near the bottom wall of the reaction vessel (121) extends out of the vessel. The extended end of the metal electrode (211) is connected to the first energized wire. The impurity separation mechanism (2) further includes a floc separation device (22), which is connected to the reaction tank (121). The floc separation device (22) includes an insoluble electrode (221) and a second energized wire. The insoluble electrode (221) is placed in the reaction tank (121). One end of the insoluble electrode (221) near the bottom wall of the reaction tank (121) extends out of the tank body. The extended end of the insoluble electrode (221) is connected to the second energized wire. The floc separation device (22) further includes a spreading device (222), which is connected to the reaction vessel (121) and an insoluble electrode (221). The spreading device (222) includes a secondary electrode (2221) and a telescopic rod (2222). The secondary electrode (2221) and the insoluble electrode (221) overlap. The secondary electrode (2221) and the insoluble electrode (221) are rotatably connected by a rotating rod. The secondary electrode (2221) and the telescopic rod (2222) are tightly connected. The end of the telescopic rod (2222) away from the secondary electrode (2221) is tightly connected to the wall of the reaction vessel (121).

2. The industrial wastewater treatment equipment with exhaust gas purification function according to claim 1, characterized in that: The colloidal separation device (21) further includes an auxiliary separation device (212), which is connected to the mounting base (11) and the reaction vessel (121). The auxiliary separation device (212) includes a drive motor (2121), a drive rotor (2122), and a drive fan blade (2123). The fixed end of the drive motor (2121) is fastened to the mounting base (11), and the output end of the drive motor (2121) is rotatably connected to the bottom of the reaction vessel (121). The driving rod (2122) is placed inside the reaction tank (121). One end of the driving rod (2122) is fixedly connected to the output end of the driving motor (2121), and the other end of the driving rod (2122) is rotatably connected to the top of the reaction tank (121). The driving fan blade (2123) is placed in the reaction tank (121). There are several driving fan blades (2123). Several driving fan blades (2123) are fixedly connected to the driving rod (2122). The driving fan blades (2123) are located at the lower third of the driving rod (2122).

3. The industrial wastewater treatment equipment with exhaust gas purification function according to claim 1, characterized in that: The impurity detection mechanism (3) includes a detection box (31), a detection light source (32), and a photoresistor (33). The impurity detection mechanism (3) is placed in the reaction vessel (121). The detection box (31) is tightly connected to the wall of the reaction vessel (121). The detection box (31) is placed in the middle position inside the reaction vessel (121). The detection light source (32) is tightly connected to the detection box (31). There are several photoresistors (33). Several photoresistors (33) are closely attached. The photoresistors (33) are tightly connected to the inner wall of the reaction vessel (121). The connecting line between the middle photoresistor (33) and the detection box (31) is on a diameter of the reaction vessel (121).

4. An industrial wastewater treatment device with an attached exhaust gas purification function according to claim 2, characterized in that: The solution separation mechanism (4) includes an inlet pipe (41), a first outlet pipe (42), a second outlet pipe (43), and a third outlet pipe (44). The inlet pipe (41) is connected to the top of the reaction tank (121). The first outlet pipe (42), the second outlet pipe (43), and the third outlet pipe (44) are connected to the upper, middle, and lower side walls of the reaction tank (121), respectively. The inlet pipe (41) is connected to the exhaust gas filtration mechanism (5).

5. An industrial wastewater treatment device with an attached exhaust gas purification function according to claim 4, characterized in that: The exhaust gas filtration mechanism (5) includes an air guide pipe (51), a semi-permeable membrane (52) and a filter chamber (53). The air guide pipe (51) is connected to the liquid inlet pipe (41). A semi-permeable membrane (52) is provided between the air guide pipe (51) and the liquid inlet pipe (41). The semi-permeable membrane (52) allows gas to pass through. The filter chamber (53) is placed on the mounting base (11). The end of the air guide pipe (51) away from the liquid inlet pipe (41) is connected to the filter chamber (53). Activated carbon is provided inside the filter chamber (53).

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