Silane coupling agent production wastewater recovery treatment device and treatment method

Abstract

The invention relates to the field of sewage treatment, and particularly discloses a silane coupling agent production wastewater recovery treatment device and a treatment method.The silane coupling agent production wastewater recovery treatment device comprises a pool body, the pool body comprises a grating pool and a slag scraping pool, and a detector for analyzing wastewater components is arranged in the grating pool; a comprehensive treatment tank is arranged between the grating tank and the slag scraping tank, and an air flotation assembly for treating wastewater is arranged in the comprehensive treatment tank; the air floatation assembly comprises a spiral frame arranged in the comprehensive treatment tank, an air floatation pipe is arranged in the spiral frame, and air spraying heads are uniformly arranged on the air floatation pipe at intervals; the comprehensive treatment tank is provided with a chemical feeding assembly for feeding chemicals, an adjusting assembly for adjusting the size of an opening of the jet head and a slag scraping assembly for scraping flocculates. The device has the effects of separating different suspended solids and reducing the recovery treatment difficulty.

Description

TECHNICAL FIELD

[0001] The present application relates to the field of sewage treatment, in particular to a silane coupling agent production wastewater recycling treatment device and method. BACKGROUND

[0002] As an important fine chemical, silane coupling agent has been widely used in the fields of building materials, energy and power, electronics, new energy vehicles, and metal ore dressing. The wastewater produced in the production process of silane coupling agent contains various pollutants, including unreacted silane compounds (such as silanol, siloxane, etc.), organic solvents (such as methanol, ethanol, acetic acid, etc.), heavy metal ions (such as chromium, nickel, lead, etc.), and oil substances. These pollutants have different physical and chemical properties, among which unreacted silane compounds have high biological toxicity and are difficult to degrade, and heavy metal ions can cause cumulative pollution to the environment.

[0003] At present, the main methods for treating silane coupling agent production wastewater include pretreatment, chemical oxidation, biological treatment, advanced treatment by physical and chemical methods, and resource recovery. In the pretreatment stage, large suspended solids are removed by a grid pool, and then the suspended solids and colloidal substances are coagulated into larger particles in the conditioning pool after coagulation and sedimentation, and a gas flotation device is used for separation. For example, the Chinese patent with publication number CN117945493B sets up a movable sleeve to make the bubbles in the conduit evenly disperse in the gas flotation cavity, accelerates the separation effect of waste residue and wastewater, and thus improves the purification efficiency. And through subsequent chemical oxidation treatment, biological treatment and other steps, the wastewater meets the discharge standard.

[0004] Because the types of suspended solids in silane coupling agent production wastewater are various and the densities are different, such as silane particles, emulsified oil, silane compounds, long-chain alcohols, etc., and the states of the flocculants formed after treatment of suspended solids with different densities are different, the flocculants formed by suspended solids with smaller density are loose and large in volume, and the flocculants formed by suspended solids with larger density are tight and small in volume. The bubbles generated by the traditional gas flotation device are too large to easily disperse the loose flocculants, and the bubbles are too small to easily reduce the floating speed of the flocculants, and the separation effect of the gas flotation device on suspended solids with different densities is poor. The subsequent treatment and separation of suspended solids are difficult, which is not conducive to the recycling of suspended solids and may cause harm to the environment. SUMMARY

[0005] In order to improve the poor separation effect of the gas flotation device on suspended solids with different densities in the prior art, which leads to difficult subsequent treatment, the present application provides a silane coupling agent production wastewater recycling treatment device and method.

[0006] The silane coupling agent production wastewater recycling treatment device provided by the present application adopts the following technical scheme: The application discloses a silane coupling agent production wastewater recycling treatment device, which comprises a pool body, the pool body comprises a grid pool and a slag scraping pool, a water inlet is formed in the grid pool, a water outlet is formed in the slag scraping pool, a detector for analyzing the components of wastewater is arranged in the grid pool, a comprehensive treatment pool is arranged between the grid pool and the slag scraping pool, and an air flotation assembly for treating wastewater is arranged in the comprehensive treatment pool. The air flotation assembly comprises a spiral frame arranged in the comprehensive treatment pool, an air flotation pipe is arranged in the spiral frame, a plurality of air injection heads are uniformly and spacedly arranged on the air flotation pipe, a pressure dissolved air tank is arranged on the side wall of the pool body, and the pressure dissolved air tank is connected with the air flotation pipe. A dosing assembly for feeding medicaments into wastewater is arranged on the comprehensive treatment pool, the dosing assembly comprises a medicament box arranged on the comprehensive treatment pool. An adjusting assembly for adjusting the opening size of the air injection head is arranged on the spiral frame, and a slag scraping assembly for scraping flocculation is arranged on the slag scraping pool.

[0007] According to the above technical scheme, because the densities of suspended matters in silane wastewater are different, after the medicaments are fed, the suspended matters with different densities form flocculation with different volumes, when the bubble diameter is close to the particle size of the flocculation, the adhesion effect is the highest, the floating speed of the flocculation can be improved, when the bubble is too large, the loose flocculation is easily dispersed, and when the bubble is too small, the floating speed of the flocculation is small; meanwhile, because the bubble size has a certain influence on the mixing effect of the medicaments, the smaller the bubble diameter is, the larger the specific surface area is, and the mixing effect of the medicaments is better, so the amount of the medicaments can be reduced.

[0008] When the silane coupling agent production wastewater is introduced into the grid pool, the grid in the grid pool screens out larger impurities, the detector in the grid pool analyzes the types and proportions of the suspended matters in the silane wastewater, the medicament box feeds the medicaments into the comprehensive treatment pool through a medicament injection pipe, the medicament box controls the medicament feeding amount according to the data of the detector, and the medicament feeding amount is matched with the content of the suspended matters in the wastewater; when the wastewater is introduced into the comprehensive treatment pool, the medicament box uniformly disperses the medicaments into the comprehensive treatment pool, the mixing effect of the medicaments and the wastewater is effectively improved, and the interference on the loose flocculation is reduced.

[0009] The pressure gas dissolving tank passes gas into the air float pipe, and forms bubbles through the air jet head arranged on the air float pipe. The adjusting assembly adjusts the opening size of the air jet head on the air float pipe, so that the size of the bubbles is distributed from small to large along the bottom to the top of the comprehensive treatment tank. The air jet head generates small bubbles first. The small bubbles are adsorbed on small flocculation bodies, the small flocculation bodies quickly float to the water surface and flow into the slag scraping tank. The small bubbles are adsorbed on large flocculation bodies. Since the adsorption effect is poor and the bubble diameter is small, the large flocculation bodies float slowly. When the large flocculation bodies float to a certain height, they are adsorbed by slightly larger bubbles generated by the air jet head. The slightly larger bubbles are adsorbed on the large flocculation bodies, so that the large flocculation bodies float to the water surface and flow into the slag scraping tank. The slag scraping assembly arranged on the slag scraping tank separates and recovers flocculation bodies of different volumes. Since the bubbles at the bottom of the comprehensive treatment tank are small, it is difficult for the small bubbles to make the precipitates float, thereby effectively accelerating the separation of the precipitates and the flocculation bodies in the wastewater. At the same time, the bubbles of different diameters make the flocculation bodies of different volumes have different floating speeds, so that the small flocculation bodies float to the water surface first, and the large flocculation bodies float to the water surface later, thereby separating the flocculation bodies of different volumes, improving the separation effect of the device, effectively improving the water quality of the treated wastewater, and reducing the harm to the environment.

[0010] Optionally, the medicine injection assembly comprises a connecting pipe arranged in the comprehensive treatment tank and rotating spirally, a medicine injection head is arranged on one end of the connecting pipe close to the spiral frame, the medicine injection head is movably matched with the spiral frame, a nozzle is arranged on the medicine injection head, a medicine injection pipe is arranged in the connecting pipe, the medicine injection pipe is in communication with the nozzle and the medicine tank respectively, a threaded rod is fixedly arranged in the comprehensive treatment tank, the threaded rod is located at the middle position of the spiral frame, and one end of the connecting pipe away from the spiral frame is arranged on the threaded rod. The medicine injection assembly further comprises a driving member for driving the connecting pipe to move.

[0011] By adopting the above technical scheme, when the driving member drives the connecting pipe to rotate on the spiral frame, the medicine injection head on the connecting pipe moves on the spiral frame, and one end of the connecting pipe away from the spiral frame rotates along the threaded rod. When the medicine injection head moves into the wastewater, the medicine in the medicine tank is introduced into the medicine injection head through the medicine injection pipe, and the medicine is sprayed into the comprehensive treatment tank through the nozzle on the medicine injection head. The medicine is sprayed to all parts of the comprehensive treatment tank by the medicine injection head spirally descending, so that the medicine and the wastewater are fully mixed. The bubbles generated by the air jet head make the medicine diffuse more quickly, thereby improving the mixing efficiency of the medicine and the wastewater. Compared with the prior art, the device reduces the interference to the just-formed flocculation bodies, and is beneficial to the formation of the flocculation bodies.

[0012] Optionally, the driving member comprises a driving pipe arranged in the comprehensive treatment tank, the threaded rod is located at the center of the driving pipe, and the driving pipe is located between the threaded rod and the spiral frame, a vertical slot is formed in the side wall of the driving pipe, the connecting pipe penetrates through the vertical slot, the connecting pipe is movably attached to the slot wall of the vertical slot, a gear ring is fixedly connected to the end of the driving pipe away from the bottom of the comprehensive treatment tank, and a first power member is arranged on the comprehensive treatment tank, and the output end of the first power member is coaxially fixedly connected with a gear engaged with the gear ring.

[0013] By adopting the above technical scheme, when the first power member drives the gear to rotate, the gear is engaged with the gear ring, the driving pipe rotates in the comprehensive treatment tank, the vertical slot on the driving pipe is abutted with the connecting pipe, and the spray head is driven to slide on the spiral frame, so that the medicament is uniformly sprayed into the comprehensive treatment tank, the end of the connecting pipe away from the spiral frame rotates along the threaded rod, the driving pipe is used to drive the connecting pipe to rotate, the interference on the just-formed flocculating body is reduced, and the flocculating body in the wastewater is beneficial to forming stable flocculating body.

[0014] Optionally, the adjusting assembly comprises a wedge-shaped block slidingly arranged in the spray head, a plurality of adjusting blocks are slidingly arranged on the spiral frame, the plurality of adjusting blocks correspond to the plurality of spray heads in one-to-one correspondence, the adjusting blocks are movably attached to the wedge-shaped block, adjusting holes are formed in the adjusting blocks, when the adjusting holes are coaxial with the axis of the spray head, the opening of the spray head is the largest, and the generated bubbles are the largest, and the adjusting assembly further comprises a synchronization member for driving the wedge-shaped block to move.

[0015] By adopting the above technical scheme, when the motor is started, the motor drives the driving pipe to rotate, the driving pipe drives the nut to move up and down on the threaded rod, when the connecting pipe rotates, the threaded rod drives the wedge-shaped block on the spray head to move through the synchronization member, and the closer the spray head is to the bottom of the comprehensive treatment tank, the longer the length of the wedge-shaped block extending.

[0016] When the driving pipe rotates, the wedge-shaped block on the spray head is abutted with the adjusting block on the spiral frame, the wedge-shaped block drives the adjusting block to move, the adjusting hole on the adjusting block is misaligned with the spray head, so as to adjust the opening size of the spray nozzle, so that the diameter of the generated bubbles is changed, the opening size of the spray head is adjusted by the adjusting block and the wedge-shaped block, the spray heads at different heights on the air floatation pipe generate bubbles with different diameters, so that the flocculating bodies with different volumes in the wastewater are adsorbed, and the flocculating bodies with different volumes are respectively floated to the water surface.

[0017] Optionally, the synchronization member comprises a nut threadedly connected to the threaded rod, the nut is provided with a driving block, the inner wall of the driving pipe is provided with a driving groove movably matched with the driving block, the end of the nut is rotatably provided with a driving wheel, the driving wheel is provided with a limiting block, the threaded rod is provided with a limiting groove movably matched with the limiting block, the connecting pipe is rotatably provided with a rotating rod, one end of the rotating rod coaxially and fixedly connected with a driven wheel near the threaded rod, the driven wheel is engaged with the driving wheel, and the wedge-shaped block is threadedly connected to one end of the rotating rod near the spiral frame.

[0018] By adopting the above technical scheme, when the driving pipe pushes the spray head to slide on the spiral frame, the driving groove rotates with the driving pipe, the driving groove abuts against the driving block, and the nut rotates, the nut rotates and lifts along the threaded rod, the limiting block on the driving wheel abuts against the limiting block on the threaded rod, the driving wheel lifts and moves along the limiting groove on the threaded rod, when the driving pipe drives the connecting pipe to rotate, the driven wheel in the connecting pipe is engaged with the driving wheel, so that the driven wheel rotates, the driven wheel drives the rotating rod to rotate, the rotating rod drives the wedge-shaped block to move a certain distance, so that the length of the wedge-shaped block is adjusted, when the connecting pipe rotates, the wedge-shaped block on the spray head abuts against the adjusting block on the spiral frame, so that the size of the opening on the spray head is adjusted, and the gas bubbles of different diameters are generated on the spray head at different heights.

[0019] Optionally, the spiral frame is slidably provided with a moving plate, the moving plate is movably matched with the adjusting block, the spiral frame is provided with an electric push rod, one end of the electric push rod is fixedly connected to the end of the moving plate, the adjusting hole is also formed in the moving plate, the electric push rod is electrically connected with the detector, and the moving plate is provided with a reset member for resetting the adjusting block.

[0020] By adopting the above technical scheme, when the detector identifies that the density and content of the suspended matter in the wastewater change, the electric push rod is started, the electric push rod drives the moving plate and the adjusting block to relatively displace, and the adjusting hole in the moving plate is dislocated from the adjusting hole in the adjusting block, so that the initial size of the opening of the spray head is adjusted, and the size range of the gas bubbles generated on the spray head is adapted to the density and content of the suspended matter in the wastewater.

[0021] Optionally, the reset member comprises a convex block arranged on the moving plate and an elastic member arranged at the end of the adjusting block, the convex block is movably matched with the adjusting block, and the convex block is separated from the adjusting block when the adjusting block is reset.

[0022] By adopting the above technical scheme, when the density and content of the suspended solids in the wastewater change, the adjusting block needs to be reset, the electric push rod is started, the electric push rod is retracted, the elastic member is compressed, when the elastic member is compressed to a certain extent, the protrusion on the electric push rod is separated from the adjusting block, the elastic member pushes the adjusting block to reset, and the elastic member returns to the original state; when the wedge-shaped block abuts against the adjusting block, the protrusion on the moving plate abuts against the adjusting block, and the force generated when the adjusting block abuts against the wedge-shaped block is much greater than the friction force between the protrusion and the adjusting block, so that when the wedge-shaped block abuts against the adjusting block, the adjusting block can move.

[0023] Optionally, the slag scraping assembly comprises a scraper arranged on the slag scraping pool, a chain is arranged on the slag scraping pool, a sprocket meshing with the chain is rotatably arranged on the slag scraping pool, a second power member for driving the sprocket to rotate is arranged on the slag scraping pool, the scraper is arranged on the chain, and two collecting pools are fixedly connected to the side wall of the slag scraping pool away from the comprehensive treatment pool, and the slag scraping assembly further comprises a guide member for guiding flocculation bodies of different sizes into the two collecting pools.

[0024] By adopting the above technical scheme, when the flocculation bodies of different sizes float to the slag scraping pool, the driving motor is started, the second power member drives the sprocket to rotate, the sprocket drives the chain to rotate, the chain drives the scraper to move, the scraper scrapes the flocculation bodies floating on the water surface into the collecting pool, and the guide member divides the flocculation bodies of different sizes and scrapes them into the two collecting pools, the flocculation bodies in the collecting pool are discharged through the slag discharge port of the bottom, the treatment of the flocculation bodies of different sizes is completed, and the separation effect of the device on different flocculation bodies is effectively improved.

[0025] Optionally, the guide member comprises a flow guide plate rotatably arranged on the pool wall of the collecting pool, two third power members are rotatably arranged on the pool wall of the collecting pool, and rotating blocks are arranged on both sides of the pool wall of the collecting pool, and the output ends of the two third power members are rotatably arranged on the rotating blocks.

[0026] By adopting the above technical scheme, the third power member is started, the output end of the third power member rotates on the rotating block and drives the flow guide plate to rotate, when the flocculation bodies of small size are scraped onto the flow guide plate, the flow guide plate member conveys the flocculation bodies into one of the collecting pools, when the scraper scrapes the flocculation bodies of large size onto the flow guide plate, the rotating direction of the flow guide plate is changed, and the flocculation bodies are guided into the other collecting pool, and the separation of the flocculation bodies of different sizes is completed.

[0027] A silane coupling agent production wastewater recycling treatment process comprises the following steps: S1, the silane coupling agent production wastewater is introduced into a grid pool, the grid pool performs preliminary treatment on the wastewater, a detector detects the wastewater after the preliminary treatment, and the density and content of the suspended solids in the wastewater are determined; S2, the first power element starts and drives the drive pipe to rotate, the drive pipe drives the spray head to descend along the spiral frame, the medicine box sprays the medicine in the comprehensive treatment tank through the spray pipe, so that the wastewater and the medicine are fully mixed, the connecting pipe rotates to the initial position at the bottom of the comprehensive treatment tank, the pressure dissolved gas tank is not opened before the connecting pipe reaches the initial position, and the opening of the air jet head is smallest at this time; S3, during the upward movement of the connecting pipe from the initial position, the pressure dissolved gas tank is opened, the air jet head generates bubbles, the drive pipe rotates on the threaded rod, at the same time, the drive pipe drives the wedge-shaped block to move through the synchronous element, so that the height of the drive pipe on the threaded rod is adapted to the length of the wedge-shaped block, when the spray head moves on the spiral frame, the wedge-shaped block abuts against the adjusting block, the adjusting hole on the adjusting block is out of position with the air jet hole, so that the air jet head at different heights generates bubbles of different diameters, and the bubbles near the bottom of the comprehensive treatment tank are smaller, during the upward movement of the spray head from the bottom to the top of the spiral frame, the small bubbles generated first are adsorbed on the flocculation bodies with smaller volume, and the flocculation bodies with smaller volume quickly rise to the water surface, the flocculation bodies with larger volume rise to a certain height and are adsorbed on the larger bubbles, and the flocculation bodies with larger volume rise to the water surface again; S4, when the density and content of suspended solids in the wastewater change, the reset element resets the adjusting block, and the electric push rod adjusts the position between the moving plate and the adjusting block again, so that the size range of the bubbles generated by the air jet head is adapted to the density and content of the suspended solids; S5, the scraper sends the flocculation bodies with different volumes to the two collection tanks in sequence, and the recycling treatment of the flocculation bodies with different volumes is completed.

[0028] In summary, the present application has at least one of the following beneficial technical effects: 1. The device identifies the content of different types of suspended solids in wastewater through the detection element, sets the air floatation pipe in the spiral frame, and moves the air jet head on the spiral frame through the driving element, adjusts the size of the opening of the air jet head on the air floatation pipe through the synchronous element, so that the air jet nozzle at different heights generates bubbles of different sizes, and the suspended solids with different volumes float to the water surface in turn, effectively improving the separation effect of suspended solids with different densities and reducing the difficulty of recycling suspended solids; 2. When the wastewater is dosed, the motor drives the drive pipe to rotate, the drive pipe drives the spray head to move in the spiral frame, the spray head sprays the medicine along the spiral frame, the bubbles generated by the air floatation pipe in the spiral pipe accelerate the mixing efficiency of the medicine and the wastewater, effectively improving the mixing efficiency of the medicine and the wastewater, reducing the interference to the just-formed flocculation bodies, and improving the efficiency of the flocculation body formation; 3. The device sets the comprehensive treatment tank, and sets the dosing assembly and the adjusting assembly in the comprehensive treatment tank, realizes the functions of dosing, stirring and air floatation of the wastewater, and reduces the occupied space of the device compared with the traditional technology. BRIEF DESCRIPTION OF DRAWINGS

[0029] Figure 1 is a schematic diagram of the overall structure of an embodiment of the present application; Figure 2 is a schematic diagram of the overall structure of an embodiment of the present application from another perspective; Figure 3 is a schematic diagram of the partial structure of an embodiment of the present application; Figure 4 is a schematic diagram of the cross-sectional structure of Figure 3 ; Figure 5 is an enlarged schematic diagram of part A in Figure 4 ; Figure 6 is a schematic diagram of the partial structure for showing the adjusting block and the moving plate; Figure 7 is a schematic diagram of the partial structure of an embodiment of the present application; Figure 8 is a schematic diagram of the partial structure of an embodiment of the present application; Figure 9 is a schematic diagram of the structure for showing the slag scraping assembly in an embodiment of the present application.

[0030] Reference signs: 1, pool body; 11, grid pool; 111, water inlet; 112, detector; 12, slag scraping pool; 121, water outlet; 13, comprehensive treatment pool; 2, air float assembly; 21, spiral frame; 22, air float pipe; 23, air jet head; 24, pressure dissolved air tank; 3, dosing assembly; 31, medicament tank; 32, threaded rod; 33, connecting pipe; 34, medicament spraying head; 35, nozzle; 36, medicament spraying pipe; 371, driving pipe; 3711, vertical groove; 372, tooth ring; 373, gear; 374, first power member; 4, adjusting assembly; 41, wedge-shaped block; 42, adjusting block; 421, adjusting hole; 431, nut; 432, driving block; 433, driving groove; 434, driving wheel; 435, limiting block; 436, limiting groove; 437, driven wheel; 438, rotating rod; 44, moving plate; 45, electric push rod; 46, reset member; 461, protruding block; 462, elastic member; 5, slag scraping assembly; 51, chain wheel; 52, chain; 53, second power member; 54, scraper; 55, collection pool; 56, guide member; 561, flow guide plate; 562, third power member. DETAILED DESCRIPTION

[0031] The following will be described in detail in combination with the accompanying Figures 1-9 The present application will be further described in detail.

[0032] The embodiment of the application discloses a silane coupling agent production wastewater recycling treatment device. Figure 1 and Figure 2 The silane coupling agent production wastewater recycling treatment device comprises a pool body 1, the pool body 1 comprises a grid pool 11, a slag scraping pool 12 and a comprehensive treatment pool 13, the comprehensive treatment pool 13 is located between the grid pool 11 and the slag scraping pool 12, the comprehensive treatment pool 13 is in communication with the grid pool 11 and the slag scraping pool 12 respectively, a lifting pump can also be arranged in the grid pool 11, the wastewater after preliminary treatment is introduced into the comprehensive treatment pool 13 through the lifting pump, a water inlet 111 is formed in the grid pool 11, a water outlet 121 is formed in the slag scraping pool 12, an electric grid is arranged in the grid pool 11, a detector 112 is arranged in the grid pool 11, the detector 112 can be a suspended five-parameter detector, an online silane special detector, an explosion-proof mud-water interface instrument and the like, a controller is arranged on the pool body 1, the controller is a programmable logic controller (PLC), a distributed control system (DCS) and the like, and the detector 112 is electrically connected with the controller.

[0033] The silane coupling agent production wastewater is introduced into the grid pool 11 through the water inlet 111, the electric grid in the grid pool 11 filters the larger solid impurities in the wastewater, the detector 112 detects and analyzes the content of the suspended matters with different densities in the wastewater and transmits data to the controller, since the sewage treatment process is continuously and discontinuously carried out, after the wastewater in the comprehensive treatment pool 13 is treated, the wastewater in the grid pool 11 is introduced into the comprehensive treatment pool 13 again for treatment.

[0034] Refer to Figures 1-4 A slag discharge port is formed in the bottom of the comprehensive treatment pool 13, a flotation assembly 2 for treating the wastewater is arranged on the pool body 1, a dosing assembly 3 for dosing agents for the wastewater is arranged on the pool body 1, and the flotation assembly 2 for aerating the wastewater is arranged.

[0035] The flotation assembly 2 comprises a spiral frame 21 fixed in the comprehensive treatment pool 13, a flotation pipe 22 is arranged in the spiral frame 21, air injection heads 23 are uniformly and intervally communicated on the flotation pipe 22, a pressure dissolved air tank 24 is fixed on the side wall of the pool body 1 and is in communication with the flotation pipe 22.

[0036] The medicine administration assembly 3 comprises a medicine tank 31 arranged on the comprehensive treatment pool 13, a threaded rod 32 is rotatably arranged in the comprehensive treatment pool 13, the threaded rod 32 is located at the center position of the spiral frame 21, a connecting pipe 33 is rotatably arranged on the threaded rod 32, the connecting pipe 33 is internally provided with a medicine spraying pipe 36, the connecting pipe 33 is connected with a medicine spraying head 34 at the end away from the threaded rod 32, the two ends of the medicine spraying pipe 36 are respectively communicated with the medicine tank 31 and the medicine spraying head 34, the medicine spraying pipe 36 is a telescopic metal pipe, the medicine spraying head 34 is movably attached to the spiral frame 21, the medicine spraying head 34 is provided with a nozzle 35, and the medicine administration assembly 3 further comprises a driving member for driving the connecting pipe 33 to move.

[0037] The driving member comprises a first power member 374 arranged on the pool body 1, which can be a servo motor, the output end of the servo motor is coaxially fixedly connected with a gear 373, a driving pipe 371 is rotatably arranged in the comprehensive treatment pool 13, a tooth ring 372 engaged with the gear 373 is welded or integrally formed on the end of the driving pipe 371 away from the bottom of the comprehensive treatment pool 13, a placing disc can be fixedly connected on the end of the driving pipe 371 close to the tooth ring 372, the medicine tank 31 is placed on the placing disc, a medicine adding port can be arranged on the top of the medicine tank 31, a pressure sensor and a liquid level sensor can be arranged in the medicine tank 31, and the pressure sensor and the liquid level sensor are electrically connected with the controller, which is beneficial to accurately control the medicine administration amount, a vertical groove 3711 is formed in the side wall of the driving pipe 371, the connecting pipe 33 penetrates through the vertical groove 3711, the connecting pipe 33 is movably attached to the vertical groove 3711, and an organ shutter can be connected between the connecting pipe 33 and the driving pipe 371, so as to reduce the waste water entering the driving pipe 371 and improve the service life of the device, and the direction of the vertical groove 3711 is parallel to the height direction of the pool body 1.

[0038] The air floatation device in the prior art uses bubbles of uniform size to adsorb and float flocculation, but flocculation bodies of different densities have different sizes, and the adsorption effect of bubbles of different sizes on flocculation bodies of different sizes is different. Larger bubbles are easy to damage flocculation bodies of larger size and loose structure, and smaller bubbles have a slower floating speed on flocculation bodies, and the specific surface area of small bubbles is larger, which can improve the reaction effect of reagents on suspended solids in wastewater, correspondingly reduce the amount of reagents, save the amount of reagents, and reduce the difficulty of subsequent recovery and treatment of excess reagents in wastewater. For example, the silane coupling agent production wastewater contains heavy metal ions and organic matter, and the flocculation bodies formed by the heavy metal ions have a diameter of 100-500 μm. The micro-bubbles with a diameter of 45-60 μm have a better floating effect on the heavy metal ions, such as zinc ions. The flocculation bodies formed by the organic matter have a diameter of 10-100 μm, and the micro-bubbles with a diameter of 45-60 μm have a poor floating effect on the flocculation bodies formed by the organic matter. The micro-bubbles with a diameter of 20-50 μm have a better adsorption effect on the flocculation bodies formed by the organic matter, but the micro-bubbles with a diameter of 20-50 μm have a poor floating effect on the heavy metal ions, such as the hydrolysis product of the silane coupling agent.

[0039] The detector 112 in the grid pool 11 detects the density and content of the wastewater, and adjusts the amount of reagents in the reagent tank 31 through the controller. When the wastewater is treated, the controller starts the first power member 374, and simultaneously opens the reagent tank 31. The first power member 374 drives the gear 373 to rotate, the gear 373 is engaged with the gear ring 372, and drives the driving pipe 371 to rotate. The vertical groove 3711 on the driving pipe 371 abuts against the connecting pipe 33, so that the spray head 34 on the connecting pipe 33 descends along the spiral frame 21. The reagents in the reagent tank 31 are introduced into the nozzle 35 through the spray pipe 36, and the nozzle 35 uniformly sprays the reagents in the comprehensive treatment pool 13 along the spiral frame 21. Compared with the prior art in which a stirring device is used to stir the reagents and wastewater, the device fully mixes the reagents and wastewater through the cooperation of the propeller and the spray head 34, reduces the interference of the stirring device on the flocculation bodies, and is beneficial to the rapid aggregation of the flocculation bodies.

[0040] When the connecting pipe 33 moves to the bottom of the comprehensive treatment pool 13, the position is the initial position of the connecting pipe 33. Before the connecting pipe 33 reaches the initial position, the pressure dissolved air tank 24 is not opened, and the air floatation pipe 22 does not generate bubbles. After the connecting pipe 33 reaches the initial position, the controller starts the pressure dissolved air tank 24 to aerate the air floatation pipe 22. At this time, the air outlet of the air jet head 23 on the air floatation pipe 22 is smallest, and the diameter of the generated bubbles is smallest.

[0041] The adjusting assembly 4 adjusts the opening size of the air jet head 23 and matches the opening size of the air jet head 23 with the height of the connecting pipe 33 on the threaded rod 32 during the upward movement of the connecting pipe 33 from the bottom of the comprehensive treatment tank 13, so that the air bubbles generated by the air jet head 23 farther away from the bottom of the comprehensive treatment tank 13 are larger; if the connecting pipe 33 does not reach the initial position, the air float pipe 22 is aerated, the reaction time of the medicament and the wastewater is shorter, and the suspended matter in the wastewater has not formed stable flocculating bodies, and if the top of the comprehensive treatment tank 13 is taken as the initial position, the large air bubbles generated are easy to disperse the loose and large flocculating bodies just formed.

[0042] During the upward movement of the connecting pipe 33 from the initial position, the small air bubbles generated by the air jet head 23 first adhere to the flocculating bodies with small volumes and make the flocculating bodies with small volumes quickly float to the water surface and flow to the slag removal tank 12, and due to the different sizes of the air bubbles generated by the air jet heads 23 at different heights, when the small air bubbles at the bottom of the comprehensive treatment tank 13 adhere to the flocculating bodies with large volumes, the flocculating bodies with large volumes float slowly, and after the flocculating bodies with large volumes float to a certain height, the slightly larger air bubbles continue to adhere to the flocculating bodies with large volumes and drive the flocculating bodies with large volumes to further float, until the flocculating bodies float to the water surface and flow to the slag removal tank 12; the device separates the flocculating bodies with different volumes by setting different sizes of air bubbles at different heights, effectively improves the separation of suspended matters with different densities, thereby reducing the difficulty of subsequent treatment of different suspended matters, effectively improves the effluent water quality of the wastewater, and reduces the harm of harmful substances in the wastewater to the environment.

[0043] Referring to Figures 5-8 The adjusting assembly 4 comprises a wedge-shaped block 41 slidably arranged on the medicament injection head 34, the medicament injection head 34 is provided with an adjusting groove in sliding fit with the wedge-shaped block 41, the spiral frame 21 is slidably provided with a plurality of adjusting blocks 42 in sliding fit with the wedge-shaped block 41, the adjusting blocks 42 correspond one-to-one to the air jet heads 23, the spiral frame 21 is slidably provided with a moving plate 44 in sliding fit with the adjusting blocks 42, and the spiral frame 21 is provided with an electric push rod 45, which is a micro electric push rod 45. The telescopic end of the electric push rod 45 is fixedly connected to the end of the moving plate 44. The adjusting blocks 42 and the moving plate 44 are both provided with adjusting holes 421, and when the adjusting holes 421 are concentric with the air jet heads 23, the air bubbles generated by the air jet heads 23 are the largest. The electric push rod 45 is electrically connected with the detector 112, and the cable connected to the electric push rod 45 is connected with the external power supply device through the inside of the spiral frame 21. The adjusting assembly 4 further comprises a synchronizing member for driving the wedge-shaped block 41 to move and a resetting member 46 for resetting the adjusting blocks 42.

[0044] The synchronizer comprises a nut 431 threadedly connected to the threaded rod 32, the nut 431 being welded or integrally formed with a driving block 432, the inside of the driving pipe 371 being provided with a driving groove 433 movably fitted with the driving block 432, the end of the nut 431 being rotatably provided with a driving wheel 434, the driving wheel 434 being welded or integrally formed with a limiting block 435, the threaded rod 32 being provided with a limiting groove 436 movably fitted with the limiting block 435, the limiting groove 436 and the driving groove 433 being parallel to the direction of the vertical groove 3711, the connecting pipe 33 being rotatably provided with a rotating rod 438, the end of the rotating rod 438 close to the threaded rod 32 being coaxially fixed with a driven wheel 437, the driven wheel 437 being engaged with the driving wheel 434, the driving wheel 434 and the driven wheel 437 both being straight bevel gears 373, a tapered block being threadedly connected to the end of the rotating rod 438 close to the spiral frame 21, the nut 431, the driving wheel 434 and the driven wheel 437 being coated with lubricating oil, grease and the like to reduce the friction between the components.

[0045] The reset member 46 comprises a protrusion 461 fixed to the moving plate 44, the protrusion 461 being an elastic protrusion 461 made of rubber, thermoplastic elastomer, polyurethane elastomer or the like, the protrusion 461 being movably fitted with the adjusting block 42, the end of the adjusting block 42 being provided with an elastic member 462, the elastic member 462 being a spring, the elastic force between the springs being smaller than the friction force between the protrusion 461 and the adjusting block 42, when the wedge-shaped block 41 abuts against the adjusting block 42, the adjusting block 42 receives a pushing force greater than the friction force between the protrusion 461 and the adjusting block 42.

[0046] Since the wastewater contains various kinds of suspended solids, different kinds of suspended solids have different densities, for example, the density ranges of two kinds of suspended solids are 0.9-1.05 g / cm³ and 0.95-1.1 g / cm³ respectively, the intersection of the density ranges of the two kinds of suspended solids is 0.95-1.05 g / cm³, the air flotation assembly 2 generates bubbles of a corresponding size for the suspended solids with a density range of 0.95-1.05 g / cm³, and takes 1 g / cm³ as a boundary, and separates the suspended solids by controlling the size of the bubbles, the device can effectively separate suspended solids with different densities, but at the same time, the processing efficiency of the suspended solids outside the density range will be reduced.

[0047] In the process of adding the medicine to the wastewater, the electric push rod 45 is first controlled to retract, the electric push rod 45 drives the moving plate 44 to move, the protrusions on the moving plate 44 abut against the adjusting block 42, and the adjusting block 42 is moved, so that the adjusting block 42 is retracted into the spiral pipe; then the first power member 374 is started, the first power member 374 drives the driving pipe 371 to rotate, so that the connecting pipe 33 reaches the bottom of the comprehensive treatment tank 13, at this time, the position of the connecting pipe 33 is the initial position, before the connecting pipe 33 reaches the initial position, the pressure dissolved air tank 24 is not opened, the air jet head 23 does not generate bubbles, and the adjusting block 42 is retracted into the spiral pipe.

[0048] When the connecting pipe 33 rises from the initial position, the controller controls the electric push rod 45 to move and push the moving plate 44 to restore the original state, the driving groove 433 on the inner wall of the driving pipe 371 is movably attached to the driving block 432 on the nut 431, the driving pipe 371 drives the nut 431 to rotate and lift on the threaded rod 32, the limiting block 435 on the driving wheel 434 is located in the limiting groove 436 on the threaded rod 32, the limiting block 435 prevents the driving wheel 434 from rotating, the driving wheel 434 moves up and down on the threaded rod 32 with the connecting pipe 33, the driven wheel 437 in the connecting pipe 33 is engaged with the driving wheel 434, so as to drive the driven wheel 437 to rotate, the driven wheel 437 drives the rotating rod 438 to rotate, the rotating rod 438 drives the wedge-shaped block 41 to move in the medicine spraying head 34, when the connecting pipe 33 rises from the initial position, the length of the wedge-shaped block 41 extending out of the adjusting groove becomes longer with the rising height.

[0049] When the connecting pipe 33 rotates, the wedge-shaped block 41 on the medicine spraying head 34 abuts against the adjusting block 42 on the spiral frame 21, the wedge-shaped block 41 pushes the adjusting block 42 to move in the spiral frame 21, the protrusions on the moving plate 44 fix the adjusting block 42, the adjusting hole 421 on the adjusting block 42 is dislocated from the air jet head 23, so as to adjust the opening size of the air jet head 23, so that the air jet head 23 close to the top of the comprehensive treatment tank 13 generates larger bubbles.

[0050] When the density and content of the suspended matter change, the air jet head 23 needs to generate bubbles with a size suitable for the density and content of the suspended matter; the electric push rod 45 is started, the electric push rod 45 drives the moving plate 44 to move, and the adjusting hole 421 on the moving plate 44 is dislocated from the air jet head 23, so as to adjust the opening size of the air jet head 23, so as to change the size range of the bubbles generated by the air jet head 23, and make the bubble size suitable for the suspended matter.

[0051] During the continuous interval treatment of wastewater, the adjusting block 42 needs to be reset, the electric push rod 45 is started, the electric push rod 45 is retracted, the moving plate 44 is moved, the moving plate 44 drives the adjusting block 42 to move through the protrusions, the spring at the end of the adjusting block 42 is compressed, when the spring is compressed to a certain degree, the adjusting block 42 and the moving plate 44 are relatively displaced, the protrusion 461 is separated from the adjusting block 42, the spring pushes the adjusting block 42 to return to the original state, so that the resetting is completed; the device adjusts the opening size of the air jet head 23 on the spiral frame 21 through the synchronous adjusting piece, so that the air jet heads 23 at different heights generate bubbles of different diameters, and different volumes of flocculation bodies are adsorbed, so that the flocculation bodies with small volumes quickly float to the water surface, the flocculation bodies with large volumes slowly float to the water surface, so that the flocculation bodies with different volumes are separated and recovered, which is beneficial to the separation and treatment of wastewater, improves the effluent quality of wastewater, and reduces the pollution of wastewater to the environment.

[0052] With reference to Figure 1 , Figure 2 and Figure 9 , the slag scraping assembly 5 comprises two groups of chain wheels 51 rotationally arranged on the slag scraping pool 12, the slag scraping pool 12 is provided with a chain 52 matched with the chain wheels 51, and a plurality of scrapers 54 are fixedly connected to the chain 52; the slag scraping pool 12 is provided with a second power piece 53, which can also be a servo motor; the output end of the second power piece 53 is coaxially fixedly connected to the chain wheel 51; two collecting pools 55 are fixedly connected to the side wall of the slag scraping pool 12; the collecting pool 55 is provided with a guide piece 56 for guiding different volumes of flocculation bodies to the two collecting pools 55 respectively; the guide piece 56 comprises a flow guide plate 561 rotationally arranged on the pool wall of the collecting pool 55, two rotating blocks are fixedly connected to the flow guide plate 561, and two third power pieces 562 are rotationally arranged on the pool wall of the collecting pool 55; the third power piece 562 can be a pneumatic cylinder; the extension ends of the two pneumatic cylinders are rotationally arranged on the two rotating blocks respectively; and a water jet pipe for flushing the flow guide plate 561 can be installed on the collecting pool 55.

[0053] When the flocculation bodies move to the water surface of the slag scraping pool 12, the second power piece 53 drives the chain wheel 51 to rotate, the chain wheel 51 drives the scrapers 54 on the chain 52 to move, the scrapers 54 scrape the flocculation bodies on the water surface, and the flocculation bodies are scraped to the flow guide plate 561; the two pneumatic cylinders are started, the electric push rod 45 controls the inclination angle of the flow guide plate 561, and different volumes of flocculation bodies on the flow guide plate 561 are introduced into the two collecting pools 55 respectively; when the flow guide plate 561 introduces different volumes of flocculation bodies into the collecting pool 55, the collecting pipe can be opened to flush the flow guide plate 561, so as to speed up the efficiency of introducing the flocculation bodies into the collecting pool 55, and reduce the mixing of different volumes of flocculation bodies on the flow guide plate 561.

[0054] The implementation principle of the silane coupling agent production wastewater recycling treatment device and treatment method is as follows: the wastewater is introduced into the grid pool 11 for preliminary treatment, the detector 112 identifies the content of different types of suspended solids in the wastewater, and the controller matches the amount of the medicament thrown by the medicament box 31 with the density and content of the suspended solids.

[0055] When the threaded rod 32 drives the connecting pipe 33 to descend to the initial position, the controller opens the medicament box 31 to throw the medicament, the medicament is sprayed into the wastewater through the spray head 34, the spray head 34 moves along the spiral rack 21 to make the medicament fully diffuse in the wastewater, and the connecting pipe 33 stirs the medicament and the wastewater, so that the medicament and the wastewater are fully mixed; when the spray head 34 moves on the spiral rack 21, the impurities adsorbed on the spiral rack 21 are scraped off, and the impurities in the wastewater are reduced to block the air jet head 23.

[0056] When the driving pipe 371 drives the connecting pipe 33 to move along the spiral rack 21, the driving pipe 371 drives the wedge-shaped block 41 on the spray head 34 to move through the synchronizer, when the spray head 34 rotates on the spiral rack 21, the wedge-shaped block 41 abuts against the adjusting block 42, the adjusting hole 421 on the adjusting block 42 is dislocated from the air jet head 23, so that the opening size of the air jet head 23 is adjusted, the air bubbles generated by the air jet head 23 are smaller when the air jet head 23 is closer to the bottom of the comprehensive treatment pool 13, so that different volumes of flocculants in the wastewater are separated, and the different volumes of flocculants are introduced into two collection pools 55 through the slag scraping assembly 5; the device identifies the content of different types of suspended solids in the wastewater through the detector 112, controls the size range of the air bubbles generated by the air float pipe 22 through the amount of the added medicament, makes the size range of the air bubbles correspond to the density interval of the suspended solids in the wastewater, and changes the opening size of the air jet head 23 through the adjusting assembly 4, so that different heights of the air jet head 23 generate different sizes of air bubbles, and different sizes of the air bubbles separate different volumes of flocculants, which effectively improves the separation effect of the suspended solids in the wastewater.

[0057] The embodiment also discloses a silane coupling agent production wastewater recycling treatment process based on the silane coupling agent production wastewater recycling treatment device. S1, the silane coupling agent production wastewater is introduced into the grid pool 11, the grid pool 11 preliminarily treats the wastewater, and the detector 112 detects the preliminarily treated wastewater to determine the density and content of the suspended solids in the wastewater; S2, the first power member 374 is started and drives the driving pipe 371 to rotate, the driving pipe 371 drives the spray head 34 to descend along the spiral rack 21, the medicament box 31 sprays the medicament in the comprehensive treatment pool 13 through the spray pipe 36, so that the wastewater and the medicament are fully mixed, the connecting pipe 33 rotates to the initial position at the bottom of the comprehensive treatment pool 13, the pressure gas dissolving tank 24 is not opened before the connecting pipe 33 reaches the initial position, and the opening of the air jet head 23 is smallest at this time. S3, during the movement of the connecting pipe 33 from the initial position upward, the pressure dissolving tank 24 is opened, the air jet head 23 generates air bubbles, the driving pipe 371 rotates on the threaded rod 32, at the same time, the driving pipe 371 drives the wedge-shaped block 41 to move through the synchronizer, so that the height of the driving pipe 371 on the threaded rod 32 is adapted to the length of the wedge-shaped block 41, when the spray head 34 moves on the spiral frame 21, the wedge-shaped block 41 abuts against the adjusting block 42, the adjusting hole 421 on the adjusting block 42 is out of position with the air jet hole, so that the air jet head 23 at different heights generates air bubbles with different diameters, and the air bubbles near the bottom of the comprehensive treatment tank 13 are smaller, during the movement of the spray head 34 from the bottom to the top of the spiral frame 21, the small air bubbles generated first are adsorbed on the flocculation bodies with small volume, and the flocculation bodies with small volume are quickly lifted to the water surface, and the flocculation bodies with large volume are adsorbed with large air bubbles after being lifted to a certain height, and the flocculation bodies with large volume are lifted to the water surface again.

[0058] S4, when the density and content of the suspended matter in the wastewater change, the reset part 46 resets the adjusting block 42, and the electric push rod 45 adjusts the position between the moving plate 44 and the adjusting block 42 again, so that the air bubbles generated by the air jet head 23 are adapted to the density and content of the suspended matter.

[0059] S5, the scraper 54 respectively scrapes the flocculation bodies with different volumes into the two collection tanks 55 in sequence, and the recycling treatment of the flocculation bodies with different volumes is completed.

[0060] The above are the preferred embodiments of the present application, and do not limit the protection scope of the present application, therefore: any equivalent changes made according to the structure, shape, principle of the present application should be covered in the protection scope of the present application.

Claims

1. A silane coupling agent production wastewater recovery treatment device, comprising a pool body (1), wherein the pool body (1) comprises a grid pool (11) and a slag scraping pool (12), a water inlet (111) is formed on the grid pool (11), and a water outlet (121) is formed on the slag scraping pool (12), characterized in that: The grid pool (11) is provided with a detector (112) for analyzing the composition of wastewater, and a comprehensive treatment pool (13) is arranged between the grid pool (11) and the slag scraping pool (12), the comprehensive treatment pool (13) is communicated with the slag scraping pool (12) and the grid pool (11), and the comprehensive treatment pool (13) is provided with a gas flotation assembly (2) for treating wastewater. The gas flotation assembly (2) comprises a spiral frame (21) arranged in the comprehensive treatment pool (13), the spiral frame (21) is provided with a gas flotation pipe (22), a plurality of air injection heads (23) are uniformly and spacedly arranged on the gas flotation pipe (22), and a pressure dissolved gas tank (24) is arranged on the side wall of the pool body (1) and communicated with the gas flotation pipe (22). The comprehensive treatment pool (13) is provided with a dosing assembly (3) for dosing agents for wastewater, and the dosing assembly (3) comprises an agent tank (31) arranged on the comprehensive treatment pool (13). The spiral frame (21) is provided with an adjusting assembly (4) for adjusting the opening size of the air injection head (23), and the slag scraping pool (12) is provided with a slag scraping assembly (5) for scraping flocculation.

2. The silane coupling agent production wastewater recovery treatment device according to claim 1, characterized by: The dosing assembly (3) comprises a connecting pipe (33) rotatably arranged in the comprehensive treatment pool (13), a medicine injection head (34) is arranged on one end of the connecting pipe (33) close to the spiral frame (21), the medicine injection head (34) is movably matched with the spiral frame (21), a nozzle (35) is arranged on the medicine injection head (34), a medicine injection pipe (36) is arranged in the connecting pipe (33), the medicine injection pipe (36) is communicated with the nozzle (35) and the agent tank (31) respectively, a threaded rod (32) is fixedly connected in the comprehensive treatment pool (13), the threaded rod (32) is located at the middle position of the spiral frame (21), one end of the connecting pipe (33) away from the spiral frame (21) is arranged on the threaded rod (32), and the dosing assembly (3) further comprises a driving member for driving the connecting pipe (33) to move.

3. The silane coupling agent production wastewater recovery treatment device according to claim 2, characterized by: The driving member comprises a driving pipe (371) rotatably arranged in the comprehensive treatment pool (13), the threaded rod (32) is located at the center position of the driving pipe (371), and the driving pipe (371) is located between the threaded rod (32) and the spiral frame (21), a vertical groove (3711) is formed in the side wall of the driving pipe (371), the connecting pipe (33) penetrates through the vertical groove (3711), the connecting pipe (33) is movably matched with the groove wall of the vertical groove (3711), a tooth ring (372) is fixedly connected to one end of the driving pipe (371) away from the bottom of the comprehensive treatment pool (13), a first power member (374) is arranged on the comprehensive treatment pool (13), and the output end of the first power member (374) is coaxially fixedly connected with a gear (373) engaged with the tooth ring (372).

4. The silane coupling agent production wastewater recovery treatment device according to claim 2, characterized by: The adjusting assembly (4) comprises a wedge-shaped block (41) slidingly arranged in the spraying head (34), a plurality of adjusting blocks (42) are slidingly arranged on the spiral frame (21), the plurality of adjusting blocks (42) correspond to the plurality of spraying heads (23) one by one, the adjusting block (42) is movably attached to the wedge-shaped block (41), the adjusting block (42) is provided with an adjusting hole (421), when the adjusting hole (421) coincides with the axis of the spraying head (23), the opening of the spraying head (23) is the largest, the bubble generated is the largest, the adjusting assembly (4) further comprises a synchronizing part for driving the wedge-shaped block (41) to move.

5. The silane coupling agent production wastewater recovery treatment device according to claim 4, characterized by: The synchronizing part comprises a nut (431) threadedly connected to the threaded rod (32), the nut (431) is provided with a driving block (432), the inner wall of the driving pipe (371) is provided with a driving groove (433) movably attached to the driving block (432), the end of the nut (431) is rotatably provided with a driving wheel (434), the driving wheel (434) is provided with a limiting block (435), the threaded rod (32) is provided with a limiting groove (436) movably attached to the limiting block (435), the connecting pipe (33) is rotatably provided with a rotating rod (438), one end of the rotating rod (438) close to the threaded rod (32) is coaxially fixedly connected with a driven wheel (437), the driven wheel (437) is engaged with the driving wheel (434), and the wedge-shaped block (41) is threadedly connected to one end of the rotating rod (438) close to the spiral frame (21).

6. The silane coupling agent production wastewater recovery treatment device according to claim 4, characterized by: The spiral frame (21) is slidingly provided with a moving plate (44), the moving plate (44) is movably attached to the adjusting block (42), the spiral frame (21) is provided with an electric push rod (45), the telescopic end of the electric push rod (45) is fixedly connected to the end of the moving plate (44), the moving plate (44) is also provided with an adjusting hole (421), the electric push rod (45) is electrically connected with the detector (112), and the moving plate (44) is provided with a resetting part (46) for resetting the adjusting block (42).

7. The silane coupling agent production wastewater recovery treatment device according to claim 6, characterized by: The resetting part (46) comprises a protrusion (461) arranged on the moving plate (44) and an elastic part (462) arranged at the end of the adjusting block (42), the protrusion (461) is movably attached to the adjusting block (42); when the adjusting block (42) is reset, the protrusion (461) is separated from the adjusting block (42).

8. The silane coupling agent production wastewater recovery treatment device according to claim 1, characterized by: The slag scraping assembly (5) comprises a scraper (54) arranged on the slag scraping pool (12), a chain (52) arranged on the slag scraping pool (12), a sprocket (51) rotatably arranged on the slag scraping pool (12) and engaged with the chain (52), a second power member (53) arranged on the slag scraping pool (12) and used for driving the sprocket (51) to rotate, and the scraper (54) is arranged on the chain (52).

9. The silane coupling agent production wastewater recovery treatment device according to claim 8, characterized by: The guide member (56) comprises a flow guide plate (561) rotatably arranged on the pool wall of the collecting pool (55), and two third power members (562) are rotatably arranged on the pool wall of the collecting pool (55).

10. A method for recovering and treating silane coupling agent production wastewater, which is suitable for use in the silane coupling agent production wastewater recovery and treatment device according to any one of claims 1 to 9, characterized by: The method comprises the following steps: S1, the silane coupling agent production wastewater is introduced into the grid pool (11), the grid pool (11) performs preliminary treatment on the wastewater, and the detector (112) detects the wastewater after the preliminary treatment to determine the density and content of the suspended solids in the wastewater; S2, the first power member (374) is started and drives the driving pipe (371) to rotate, the driving pipe (371) drives the medicine spraying head (34) to descend along the spiral frame (21), the medicine tank (31) sprays the medicine into the comprehensive treatment pool (13) through the medicine spraying pipe (36), so that the wastewater and the medicine are fully mixed, the connecting pipe (33) is in the initial position when it rotates to the bottom of the comprehensive treatment pool (13), the pressure gas dissolving tank (24) is not opened before the connecting pipe (33) reaches the initial position, and the opening of the air jet head (23) is smallest at this time; S3, during the upward movement of the connecting pipe (33) from the initial position, the pressure gas dissolving tank (24) is opened, the air jet head (23) generates bubbles, the driving pipe (371) rotates on the threaded rod (32) at the same time, the driving pipe (371) moves the wedge-shaped block (41) through the synchronous member, so that the height of the driving pipe (371) on the threaded rod (32) is matched with the length of the wedge-shaped block (41), the wedge-shaped block (41) abuts against the adjusting block (42) when the medicine spraying head (34) moves on the spiral frame (21), the adjusting hole (421) on the adjusting block (42) is dislocated from the air jet hole, so that the air jet head (23) at different heights generates bubbles with different diameters, and the bubbles near the bottom of the comprehensive treatment pool (13) are smaller, during the upward movement of the medicine spraying head (34) from the bottom to the top of the spiral frame (21), the small bubbles are adsorbed on the small flocculation bodies, and the small flocculation bodies rapidly rise to the water surface, the large flocculation bodies are adsorbed on the large bubbles when rising to a certain height, and the large flocculation bodies rise to the water surface again; S4, when the density and content of suspended solids in wastewater change, the reset member (46) resets the adjusting block (42), the electric push rod (45) re-adjusts the position between the moving plate (44) and the adjusting block (42), so that the size range of the bubbles generated by the air jet head (23) is adapted to the density and content of the suspended solids; S5, the scraper (54) respectively scrapes different volumes of flocculation bodies into two collection tanks (55) in sequence, and completes the recovery treatment of different volumes of flocculation bodies.

Images