Multi-channel drainage equipment for glow cracking sewage treatment

By adopting multi-channel drainage equipment in glow cracking sewage treatment equipment, combining rotary precipitation and real-time NTU numerical detection, the problems of low treatment efficiency and high operation and maintenance costs in the prior art are solved, and more efficient sewage treatment and the effect of reducing operation and maintenance costs are achieved.

CN119874139APending Publication Date: 2025-04-25山东晟博环境科技有限公司
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Patent Information

Application Number
CN202510379003.9
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2025-03-28
Publication Date
2025-04-25

AI Technical Summary

Technical Problem

The drainage structure of existing glow cracking sewage treatment equipment has problems of low treatment efficiency and high operation and maintenance costs. Especially when treating sewage with different water quality, it is easy to cause the catalyst active site to be wrapped in suspended substances, reduce the TOC removal rate, and may cause equipment failure due to excessive coagulant injection.

Method used

Multi-channel drainage equipment is adopted, including a precipitation barrel, a liquid separation barrel and multiple turbidity sensors. Through rotary precipitation and real-time NTU numerical detection, sewage is introduced into different sewage treatment tanks, and the amount of coagulant is delivered in real time according to the NTU numerical value of sewage.

Benefits of technology

It improves the treatment efficiency of glow cracking sewage treatment equipment, reduces operation and maintenance costs, avoids equipment failures caused by excessive coagulant agents, and improves the impurity separation effect of sewage, reducing chemical pollution risks and production costs.

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Abstract

The invention relates to multi-channel drainage equipment for glow cracking sewage treatment, which relates to the technical field of sewage drainage, and comprises a pedestal, a settling barrel arranged at the side part of a rack, a water inlet pipe, a water outlet pipe and a flow guide pipe connected to the settling barrel, a turbidity sensor mounted in a liquid separation barrel, a first liquid separation pipe connected to the liquid separation barrel, and a second liquid separation pipe connected to the second liquid separation pipe, the first liquid distribution pipe and the second liquid distribution pipe are respectively connected with a first sewage treatment tank and a second sewage treatment tank, the first sewage treatment tank and the second sewage treatment tank are jointly connected with a coagulant aid input pipe, and the first sewage treatment tank and the second sewage treatment tank are respectively provided with a first liquid delivery pipe and a second liquid delivery pipe. The glow cracking sewage treatment equipment is provided with a multi-channel drainage structure, the front-end drainage can perform preliminary impurity separation on sewage, and the rear-end drainage can control the putting amount of a coagulant aid according to the NTU value of the sewage, so that the treatment efficiency of the glow cracking sewage treatment equipment is improved, meanwhile, equipment faults caused by excessive coagulant aid can be avoided, and the operation and maintenance cost is reduced.
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Description

Technical Field

[0001] The invention relates to the technical field of sewage drainage, and in particular discloses a multi-channel drainage device for glow cracking sewage treatment. Background Art

[0002] The glow pyrolysis wastewater treatment equipment is an advanced oxidation equipment based on plasma technology. It excites air or water molecules in the reaction chamber through a high-voltage electric field (10-50kv) to produce high-energy active substances, thereby efficiently degrading difficult-to-degrade organic matter, killing microorganisms and decomposing microplastics. It is mainly used in high-difficulty scenarios such as pharmaceutical wastewater, electronic wastewater, textile wastewater and industrial hazardous waste. The effluent from the glow pyrolysis wastewater treatment equipment can be directly reused or discharged in compliance with standards. It is particularly suitable for industrial parks and pharmaceutical companies with strict requirements on water quality.

[0003] The utility model with application announcement number: CN210559564U discloses a novel drainage device for chemical sewage treatment. The prior art is provided with a sewage outlet for discharging sewage. The sewage in the sewage pool can be discharged through the sewage outlet, thereby achieving the purpose of sewage drainage. The invention with application announcement number: CN108911067A discloses a medical sewage disinfection discharge drainage device. The prior art is provided with a connecting pipe and a drainage pipe. The sewage and the medicine solution can be stirred and mixed by setting a stirring shaft, and the mixed solution is caused to flow into the connecting pipe by controlling the first support plate and the second support plate, so that it is discharged from the drainage pipe.

[0004] The drainage structures disclosed in the prior art are all single-channel drainage structures, and the drainage channel can only drain sewage with a single NTU value. The NTU value is the turbidity parameter of sewage. If the sewage contains a large amount of silt and large particles of impurities, the NTU value of the sewage will be in a higher range. Since the glow cracking wastewater treatment equipment has relatively strict requirements on the NTU value of sewage, it is necessary to control the NTU value of sewage below 50NTU. If the NTU value of sewage is high, it will cause the treatment efficiency of the glow cracking equipment to decrease by 30%-60%, increase energy consumption by 20%-30%, and significantly shorten the life of the equipment; therefore, it is necessary to pre-treat the sewage in advance, and the NTU value of the sewage can be effectively reduced by adding a coagulant. If the glow cracking wastewater treatment equipment adopts the single-channel drainage structure in the above-mentioned prior art, the sewage enters the drainage device through a single channel and flows out through a single channel, which is difficult to adapt to different water qualities (such as high-concentration pharmaceutical wastewater and low-concentration domestic sewage). After mixing, the active sites of the catalyst may be wrapped by suspended matter, causing the TOC removal rate to decrease by 20%-40%, affecting the treatment efficiency of the glow cracking wastewater treatment equipment; and if the amount of coagulant added is too high, it is very easy to cause equipment failure (such as electrode ablation, pipeline blockage), which will directly lead to production suspension in severe cases, increase operation and maintenance costs, and increase the comprehensive operating costs by 25%-40%. Summary of the invention

[0005] In view of the problems of low treatment efficiency and high operation and maintenance cost of the drainage structure of the current auxiliary glow cracking wastewater treatment equipment, the present invention provides a multi-channel drainage equipment for glow cracking wastewater treatment.

[0006] To solve the above problems, the present invention provides the following technical solutions: A multi-channel drainage device for glow cracking wastewater treatment, comprising a pedestal, a frame is fixedly mounted on the pedestal, a sedimentation barrel is fixedly arranged on the side of the frame, the sedimentation barrel is used for preliminarily separating sewage from large particles of impurities, a water inlet pipe for sewage to enter is fixedly connected to the top of the sedimentation barrel, a water outlet pipe for upper sewage to pass through is fixedly connected to the top side wall of the sedimentation barrel, a guide pipe is connected to the bottom of the sedimentation barrel, a liquid separation barrel is fixedly hoisted on the inner side of the frame, the inner cavity of the liquid separation barrel is connected to the water outlet pipe, a plurality of turbidity sensors are installed in the liquid separation barrel, the turbidity sensors are used to detect the NTU value of the sewage in the liquid separation barrel, and the liquid separation barrel is fastened with a first liquid separation pipe, a second liquid separation pipe, and a second liquid separation pipe. Liquid dispensing tube, the NTU value of sewage flowing in the first liquid dispensing tube is greater than that in the second liquid dispensing tube, the first liquid dispensing tube and the second liquid dispensing tube are respectively connected to the first sewage treatment tank and the second sewage treatment tank, the first sewage treatment tank and the second sewage treatment tank are both tightly connected to the pedestal, the first sewage treatment tank and the second sewage treatment tank are commonly connected to a coagulant input pipe, the coagulant input pipe inputs the coagulant according to the NTU value of the sewage in the first sewage treatment tank and the second sewage treatment tank, the first liquid delivery pipe and the second liquid delivery pipe are respectively tightly installed on the outer walls of the first sewage treatment tank and the second sewage treatment tank, the first liquid delivery pipe and the second liquid delivery pipe are both connected to the liquid inlet pipeline of the glow cracking sewage treatment equipment.

[0007] Preferably, a first mounting block is fixedly installed on the side of the frame, a second mounting block fastened to the first mounting block is fixedly installed on the outer wall of the sedimentation barrel, an upper float chamber and a sedimentation chamber distributed up and down are provided in the sedimentation barrel, the inner diameter of the upper float chamber is larger than that of the sedimentation chamber, the water inlet pipe and the water outlet pipe are both connected with the upper float chamber, the guide pipe is connected with the sedimentation chamber, a rotating rod is rotatably provided in the upper float chamber, a propeller impeller is fixedly mounted on the bottom end of the rotating rod, and the propeller impeller is arranged between the upper float chamber and the sedimentation chamber.

[0008] Preferably, a base is fixedly installed on the top of the sedimentation barrel, a first motor is fixedly installed on the base, the output shaft of the first motor is transmission-connected to a rotating rod, a propeller blade is arranged on the outer side of the rotating rod, a plurality of mounting rods are fixedly arranged on the outer wall of the rotating rod, each mounting rod is provided with a slot, a cap is fixedly installed on the outer side of the slot, the slot is fastened to the propeller blade, and the rotation radius of the propeller blade is smaller than that of the propeller impeller.

[0009] Preferably, a first solenoid valve is installed on the water inlet pipe, a second solenoid valve and a first centrifugal pump are installed on the water outlet pipe, the bottom of the first centrifugal pump is firmly connected to the pedestal, and a second motor is mounted on the top of the first centrifugal pump.

[0010] Preferably, a hanging frame is fixedly installed on the inner top of the frame, the bottom of the hanging frame is tightly connected to the outer wall of the liquid dispensing barrel, the third solenoid valve and the fourth solenoid valve are respectively installed on the pipelines of the first liquid dispensing tube and the second liquid dispensing tube, a stabilizing frame is fixedly installed on the base, a plurality of pipe seats are fixedly installed on the top of the stabilizing frame, and the pipe seats are used to stably arrange the first liquid dispensing tube and the second liquid dispensing tube.

[0011] Preferably, a buffer box is fixedly installed on the pedestal, an opening is provided on the top of the buffer box, a bracket is fixedly installed on the side of the buffer box, a drainage box is fastened on the bracket, the drainage box is arranged above the opening, a second centrifugal pump and a fifth solenoid valve are installed on the pipeline of the guide pipe, a third motor is fixedly installed on the top of the second centrifugal pump, and the liquid outlet port of the guide pipe is vertically arranged downward and arranged above the drainage box.

[0012] Preferably, a frame is fixedly mounted on the top periphery of the buffer box, a screening box is provided on the inner side of the frame, the screening box is arranged above the opening, an inclined curved portion is provided on the side of the drainage box close to the opening, the inclined curved portion is arranged above the screening box, a plurality of evenly arranged sieve holes are provided on the bottom of the screening box, the passing area of ​​the sieve holes is smaller than the opening, and handles are fixedly installed on both sides of the screening box.

[0013] Preferably, the side of the buffer box is connected to the first infusion tube and the second infusion tube, and the sixth solenoid valve and the seventh solenoid valve are respectively installed on the pipelines of the first infusion tube and the second infusion tube, and the first infusion tube and the second infusion tube are commonly connected to a junction pipe, and a third centrifugal pump is installed on the pipeline of the junction pipe, and a fourth motor is installed on the top of the third centrifugal pump, and the junction pipe is connected to the first sewage treatment tank; a first leakage pipe is installed at the bottom of the buffer box, and the arrangement height of the first leakage pipe is lower than that of the first infusion tube and the second infusion tube, and an eighth solenoid valve is installed on the pipeline of the first leakage pipe.

[0014] Preferably, NTU numerical sensors are fixedly installed on the outside of the first sewage treatment tank and the second sewage treatment tank, the liquid outlet port of the coagulant input pipe is fastened with a three-way pipe, the two liquid outlet ports of the three-way pipe are respectively connected to the first diversion pipe and the second diversion pipe, the first diversion pipe and the second diversion pipe are respectively installed on the pipelines, and the first diversion pipe and the second diversion pipe are respectively connected to the first sewage treatment tank and the second sewage treatment tank.

[0015] Preferably, support legs are fixedly installed on the outer walls of the first sewage treatment tank and the second sewage treatment tank, and the bottom ends of the support legs are tightly connected to the pedestal. The second drainage pipe and the third drainage pipe are respectively installed at the bottom of the first sewage treatment tank and the second sewage treatment tank, and the arrangement heights of the second drainage pipe and the third drainage pipe are lower than the first liquid delivery pipe and the second liquid delivery pipe. The eleventh solenoid valve and the twelfth solenoid valve are respectively fixedly installed on the pipelines of the first liquid delivery pipe and the second liquid delivery pipe, and the thirteenth solenoid valve and the fourteenth solenoid valve are respectively fixedly installed at the liquid outlet ports of the second drainage pipe and the third drainage pipe.

[0016] Compared with the prior art, the present invention has the following beneficial effects: 1. The sedimentation barrel in the present invention can perform rotary sedimentation on the sewage injected from the water inlet pipe, so that the sewage is initially rotated and separated in the sedimentation barrel, and the sewage on the upper layer of the sedimentation barrel enters the liquid separation barrel. By setting a turbidity sensor, the sewage in the liquid separation barrel can be detected in real time by NTU value, so that sewage with different NTU values ​​enters the first liquid separation pipe and the second liquid separation pipe respectively according to the standard value, so that it is finally injected into the first sewage treatment tank and the second sewage treatment tank, and through the real-time detection ability of the NTU value sensor, appropriate coagulant is injected into the first sewage treatment tank and the second sewage treatment tank through the first shunt pipe and the second shunt pipe, so that the sewage is continuously input into the glow cracking sewage treatment equipment through the first liquid delivery pipe and the second liquid delivery pipe respectively. The present invention is provided with a multi-channel drainage structure, and the sewage can be initially separated from impurities during the front-end drainage process, and the amount of coagulant can be controlled according to the NTU value of the sewage during the rear-end drainage process, which not only improves the treatment efficiency of the glow cracking sewage treatment equipment, but also avoids equipment failure caused by excessive coagulant, and reduces operation and maintenance costs; 2. The present invention can effectively adapt the rotating rod and the propeller impeller by arranging the upper floating chamber and the sedimentation chamber with different inner diameters in the sedimentation barrel, so as to perform cyclone sedimentation treatment on the sewage in the sedimentation barrel, so that the large particles of impurities in the sewage are precipitated to the bottom of the sedimentation chamber. This can not only accelerate the sedimentation rate of the sewage in the sedimentation barrel, but also accelerate the sewage at the top of the upper floating chamber to flow into the outlet pipe under the coordinated rotation of the propeller blades, thereby improving the circulation rate of the sewage in the equipment, shortening the drainage process of the glow cracking sewage treatment equipment, and further improving the treatment capacity of the glow cracking sewage treatment equipment, so as to adapt to high-flow and high-load sewage treatment scenarios; 3. The drainage box in the present invention can buffer and drain the sewage flowing out of the sedimentation chamber in the sedimentation barrel, and effectively separate the large-particle impurities mixed in the sewage by cooperating with the screening box, so that the impurities precipitated from the bottom layer of the sewage in the buffer box are all small-particle impurities, and by setting the first liquid delivery pipe and the second liquid delivery pipe, the top layer of sewage in the buffer box is delivered to the first sewage treatment tank, thereby realizing multi-level sedimentation treatment operations. This technical feature can greatly improve the impurity separation effect of sewage in the front-end drainage process of the present invention, thereby reducing the amount of coagulant added at the back end. On the one hand, it can reduce the risk of chemical pollution and avoid damage to the environment. On the other hand, it effectively reduces the production cost, thereby achieving scientific delivery and enhancing the drainage equipment in the present invention The ability to resist water quality fluctuations, therefore, has a very broad application prospect. BRIEF DESCRIPTION OF THE DRAWINGS

[0017] In order to more clearly illustrate the technical solution of the present invention, the following briefly introduces the drawings required for the description. Obviously, the drawings described below are only some embodiments of the present invention. For those skilled in the art, other drawings can be obtained based on these drawings without creative work. Figure 1 It is a schematic diagram of the overall device structure of the present invention; Figure 2 This is a schematic diagram of the installation structure of the sedimentation barrel and the liquid separation barrel of the present invention; Figure 3 It is a schematic diagram of the installation structure of the second solenoid valve and the fifth solenoid valve of the present invention; Figure 4 This is a schematic diagram of the internal structure of the sedimentation barrel of the present invention; Figure 5 It is a schematic diagram of the installation structure of the propeller impeller and propeller blades of the present invention; Figure 6 It is a schematic diagram of the installation structure of the third solenoid valve and the fourth solenoid valve of the present invention; Figure 7 It is a schematic diagram of the internal structure of the liquid separation barrel of the present invention; Figure 8 This is a schematic diagram of the installation structure of the buffer box of the present invention; Fig. 9 It is a schematic diagram of the arrangement structure of the drainage box and the screening box of the present invention; Fig.10 This is a schematic diagram of the installation structure of the first infusion tube and the second infusion tube of the present invention; Fig.11 It is a schematic diagram of the internal structure of the screening box of the present invention; Fig.12 This is a schematic diagram of the installation structure of the first sewage treatment tank and the second sewage treatment tank of the present invention; Fig.13 It is a schematic diagram of the installation structure of the first shunt pipe and the second shunt pipe of the present invention; In the figure: 1. base, 2. frame, 3. sedimentation barrel, 4. water inlet pipe, 5. water outlet pipe, 6. guide pipe, 7. liquid separation barrel, 8. turbidity sensor, 9. first liquid separation pipe, 10. second liquid separation pipe, 11. first sewage treatment tank, 12. second sewage treatment tank, 13. coagulant input pipe, 14. first liquid delivery pipe, 15. second liquid delivery pipe, 16. first mounting block, 17. second mounting block, 18. upper floating chamber, 19. sedimentation chamber, 20. rotating rod, 21. propeller impeller, 22. base, 23. first motor, 24. propeller blade, 25. mounting rod, 26. slot, 27. cap, 28. first solenoid valve, 29. second solenoid valve, 30. first centrifugal pump, 31. second motor, 32. lifting frame, 33. third solenoid valve, 34. fourth solenoid valve, 35. stabilizer Fixed frame, 36. Pipe seat, 37. Buffer box, 38. Opening, 39. Bracket, 40. Drainage box, 41. Second centrifugal pump, 42. Fifth solenoid valve, 43. Third motor, 44. Frame, 45. Screening box, 46. Oblique bend, 47. Sieve hole, 48. Handle, 49. First infusion tube, 50. Second infusion tube, 51. Sixth solenoid valve, 52. Seventh solenoid valve, 53. Converging pipe, 54. Third centrifugal pump, 55. Fourth motor, 56. Drain pipe, 57. Eighth solenoid valve, 58. NTU numerical sensor, 59. Three-way pipe, 60. First shunt pipe, 61. Second shunt pipe, 62. Ninth solenoid valve, 63. Tenth solenoid valve, 64. Support leg, 65. Second drain pipe, 66. Third drain pipe, 67. Eleventh solenoid valve, 68. Twelfth solenoid valve. 69. The thirteenth solenoid valve, 70. The fourteenth solenoid valve. DETAILED DESCRIPTION

[0018] In order to make the purpose, features and advantages of the present invention more obvious and easy to understand, the technical scheme of the present invention will be clearly and completely described below in conjunction with the drawings in this specific embodiment. Obviously, the embodiments described below are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0019] This specific embodiment provides a multi-channel drainage device for glow pyrolysis wastewater treatment, such as Figure 1-Figure 13 As shown; it includes a pedestal 1, and vibration cushions are fixedly installed at the four corners of the bottom of the pedestal 1, so as to reduce the vibration frequency of the whole equipment. A frame 2 is fixedly installed on the table plate at the top of the pedestal 1, and the frame 2 is arranged on the left side of the pedestal 1. The bottom of the frame 2 is fastened to the table plate at the top of the pedestal 1; a sedimentation barrel 3 is fixedly installed on the right side of the frame 2, and a first mounting block 16 is fixedly installed on the right side of the frame 2. The first mounting block 16 is provided with two and arranged up and down, and a second mounting block 17 is fixedly installed on the left outer wall of the sedimentation barrel 3. The second mounting block 17 is provided with two and corresponds to the first mounting block 16 one by one, and the first mounting block 16 and the second mounting block 17 can be fastened and connected by bolts, so that the sedimentation barrel 3 can be stably loaded to the right side of the frame 2.

[0020] The sedimentation barrel 3 is provided with an upper floating chamber 18 and a sedimentation chamber 19 which are distributed up and down. The inner diameter of the upper floating chamber 18 is larger than that of the sedimentation chamber 19. The top of the sedimentation barrel 3 is fixedly connected with an inlet pipe 4 for sewage to enter. A first solenoid valve 28 is installed on the pipeline of the inlet pipe 4 to control the flow rate of sewage entering the inlet pipe 4. The liquid outlet port of the inlet pipe 4 is arranged in the upper floating chamber 18, so that the inlet pipe 4 injects sewage from the upper floating chamber 18 into the inner cavity of the sedimentation barrel 3.

[0021] A rotating rod 20 is rotatably arranged in the upper floating chamber 18, a base 22 is fixedly installed on the top of the sedimentation barrel 3, a first motor 23 is fixedly installed on the base 22, and the output shaft of the first motor 23 is arranged downward and is transmission-connected with the top of the rotating rod 20, so that the output shaft of the first motor 23 drives the rotating rod 20 to rotate in the sedimentation barrel 3. A propeller 21 is fixedly sleeved on the bottom end of the rotating rod 20, and the propeller 21 is arranged between the upper floating chamber 18 and the sedimentation chamber 19. The propeller 21 can rotate with the rotating rod 20 and stir the sewage, so that large particles of impurities in the sewage are precipitated to the bottom of the sedimentation chamber 19. The outer side of the rotating rod 20 is provided with a propeller blade 24, which is a continuous integrated structure; a plurality of mounting rods 25 are fixedly provided on the outer wall of the rotating rod 20, and the mounting rods 25 are arranged vertically with the rotating rod 20. A slot 26 is provided inside each mounting rod 25, and the inner wall of the slot 26 contacts the outer wall of the propeller blade 24, so that the slot 26 and the propeller blade 24 are fastened and engaged, thereby fixing the propeller blade 24 on the outer periphery of the rotating rod 20, so that the propeller blade 24 rotates with the rotating rod 20, and the rotation radius of the propeller blade 24 is smaller than the propeller impeller 21, so as to assist the propeller impeller 21 and accelerate the precipitation rate of large particles of impurities in the sewage. A cap 27 is fixedly installed on the outer side of the slot 26, so as to prevent the propeller blade 24 from falling off the mounting rod 25 and ensure the stability of the installation of the rotating rod 20 and the propeller blade 24.

[0022] The top side wall of the sedimentation barrel 3 is fixedly connected with an outlet pipe 5 for the upper sewage to pass through, and the liquid inlet port of the outlet pipe 5 is connected with the upper floating chamber 18, so that the sewage in the upper floating chamber 18 flows into the outlet pipe 5. The bottom of the sedimentation barrel 3 is connected with a guide pipe 6, and the liquid inlet port of the guide pipe 6 is connected with the sedimentation chamber 19, so that the large particle impurities in the sedimentation chamber 19 enter the guide pipe 6 along with the sewage. A hanging frame 32 is fixedly installed on the inner top of the frame 2, and the bottom of the hanging frame 32 is tightly connected to the outer wall of the liquid separation barrel 7. The liquid separation barrel 7 is arranged horizontally and is provided with an internal cavity. A second solenoid valve 29 and a first centrifugal pump 30 are installed on the pipeline of the water outlet pipe 5. The bottom of the first centrifugal pump 30 is tightly connected to the pedestal 1, and a second motor 31 is installed on the top of the first centrifugal pump 30. The liquid outlet port of the water outlet pipe 5 is connected to the liquid separation barrel 7. Sewage can be continuously injected into the liquid separation barrel 7 under the action of the first centrifugal pump 30 and the second motor 31, and the sewage flow is controlled by the second solenoid valve 29.

[0023] A plurality of turbidity sensors 8 are installed in the liquid separation barrel 7. There are three turbidity sensors 8 in total and they are evenly arranged in a ring shape. One end of the sensing head of each turbidity sensor 8 is arranged in the inner cavity of the liquid separation barrel 7, and the other end is arranged outside the liquid separation barrel 7, so as to be conveniently connected to an external control device, so as to be used for real-time detection of the NTU value of the sewage in the liquid separation barrel 7. The liquid separation barrel 7 is tightly connected to the first liquid separation pipe 9 and the second liquid separation pipe 10. The third solenoid valve 33 and the fourth solenoid valve 34 are respectively installed on the pipelines of the first liquid separation pipe 9 and the second liquid separation pipe 10. The third solenoid valve 33 and the fourth solenoid valve 34 control the flow of sewage in the first liquid separation pipe 9 and the second liquid separation pipe 10, respectively. The NTU value of the sewage flowing in the first dispensing tube 9 is greater than that in the second dispensing tube 10. The operator can set a standard NTU value. When the NTU value of the sewage in the dispensing barrel 7 is greater than the standard value, it can flow out through the first dispensing tube 9. When the NTU value of the sewage in the dispensing barrel 7 is less than the standard value, it can flow out through the second dispensing tube 10, thereby realizing real-time diversion.

[0024] A stabilizing frame 35 is fixedly mounted on the pedestal 1, and the stabilizing frame 35 is arranged on the right side of the frame 2. The bottom of the stabilizing frame 35 is tightly connected to the table top of the pedestal 1. A plurality of pipe seats 36 are fixedly mounted on the top of the stabilizing frame 35. There are two pipe seats 36 in total. The two pipe seats 36 can stably arrange the first liquid dispensing pipe 9 and the second liquid dispensing pipe 10 on the top of the stabilizing frame 35, respectively, so as to improve the stability of the overall equipment. The first solenoid valve 28 installed on the pipeline of the water inlet pipe 4 can be tightly connected to the top of the stabilizing frame 35, so as to enhance the stability of the installation of the water inlet pipe 4.

[0025] The first sewage treatment tank 11 and the second sewage treatment tank 12 are arranged in sequence on the right side of the stabilizing frame 35. The outer walls of the first sewage treatment tank 11 and the second sewage treatment tank 12 are fixedly mounted with support legs 64. The bottom of each support leg 64 is tightly connected to the table plate at the top of the pedestal 1, so that the first sewage treatment tank 11 and the second sewage treatment tank 12 are fixedly mounted on the pedestal 1. The first liquid dispensing pipe 9 and the second liquid dispensing pipe 10 are respectively connected to the first sewage treatment tank 11 and the second sewage treatment tank 12. The liquid outlet ports of the first liquid dispensing pipe 9 and the second liquid dispensing pipe 10 are respectively arranged at the top of the first sewage treatment tank 11 and the second sewage treatment tank 12, so that the sewage is injected from the top of the first sewage treatment tank 11 and the second sewage treatment tank 12 into their respective inner cavities.

[0026] A buffer box 37 is provided at the rear side of the first sewage treatment tank 11 and the second sewage treatment tank 12, and the bottom of the buffer box 37 is tightly connected to the table top of the pedestal 1. A second centrifugal pump 41 and a fifth solenoid valve 42 are installed on the pipeline of the guide pipe 6, and a third motor 43 is fixedly installed on the top of the second centrifugal pump 41. The liquid outlet port of the guide pipe 6 is vertically downward and arranged above the buffer box 37. By providing the second centrifugal pump 41 and the third motor 43, the mixed solution of sewage and large particle impurities at the bottom of the sedimentation chamber 19 can be transported to the guide pipe 6, and the flow rate of the mixed solution is controlled by the fifth solenoid valve 42. The top of the buffer box 37 is provided with an opening 38, and a bracket 39 is fixedly installed on the side of the buffer box 37. The top of the bracket 39 is higher than the buffer box 37, and a drainage box 40 is fastened and installed above the bracket 39; the drainage box 40 is an open structure, and its top and the side close to the buffer box 37 are open openings; the liquid outlet port of the guide pipe 6 is arranged above the drainage box 40, and the mixed solution in the guide pipe 6 can directly enter the drainage box 40. A frame 44 is fixedly sleeved on the top periphery of the buffer box 37, and the arrangement height of the frame 44 is higher than the outer edge of the buffer box 37, so as to prevent the mixed solution flowing out of the guide pipe 6 from overflowing the buffer box 37. A screening box 45 is provided inside the frame 44, and the screening box 45 is arranged above the opening 38. A slanted portion 46 is provided on the side of the drainage box 40 close to the opening 38, and the slanted portion 46 is provided above the screening box 45. The slanted portion 46 can facilitate the introduction of the mixed solution into the screening box 45. The bottom of the screening box 45 is provided with a plurality of sieve holes 47 evenly arranged, and the passing area of ​​the sieve holes 47 is smaller than the opening 38, so that the sieve holes 47 isolate the large particles of impurities in the mixed solution in the screening box 45, and the sewage without large particles of impurities flows into the buffer box 37; handles 48 are fixedly installed on both sides of the screening box 45, so that the operator can carry the screening box 45 for cleaning.

[0027] The top of the side of the buffer tank 37 is connected with a first infusion tube 49 and a second infusion tube 50. The liquid inlet ports of the first infusion tube 49 and the second infusion tube 50 are arranged inside the buffer tank 37. The first infusion tube 49 and the second infusion tube 50 are respectively installed with a sixth solenoid valve 51 and a seventh solenoid valve 52. The sixth solenoid valve 51 and the seventh solenoid valve 52 can be used to control the flow in the first infusion tube 49 and the second infusion tube 50. The first infusion tube 49 and the second infusion tube 50 are connected together with a manifold 53. A third centrifugal pump 54 is installed on the manifold 53. A fourth motor 55 is installed on the top of the third centrifugal pump 54. The manifold 53 is connected with the first sewage treatment tank 11, so that the sewage at the top of the buffer tank 37 is introduced into the first sewage treatment tank 11. A first drainage pipe 56 is installed at the bottom of the buffer box 37. The arrangement height of the first drainage pipe 56 is lower than the first infusion pipe 49 and the second infusion pipe 50. The sewage at the bottom of the buffer box 37 contains some small particles of impurities, and the sewage containing small particles of impurities can be discharged from the buffer box 37 through the first drainage pipe 56; an eighth solenoid valve 57 is installed on the pipeline of the first drainage pipe 56 to control the flow rate of the discharge of the buffer box 37.

[0028] The first sewage treatment tank 11 and the second sewage treatment tank 12 are connected to a coagulant input pipe 13, which can be connected to an external coagulant delivery device, so that the coagulant is continuously input into the coagulant input pipe 13. The liquid outlet port of the coagulant input pipe 13 is tightly connected to a tee pipe 59, and the two liquid outlet ports at the bottom of the tee pipe 59 are respectively connected to a first shunt pipe 60 and a second shunt pipe 61, and the pipelines of the first shunt pipe 60 and the second shunt pipe 61 are respectively installed with a ninth solenoid valve 62 and a tenth solenoid valve 63, and the first shunt pipe 60 and the second shunt pipe 61 are respectively connected to the first sewage treatment tank 11 and the second sewage treatment tank 12, so that the ninth solenoid valve 62 and the tenth solenoid valve 63 control the flow of the coagulant in the first shunt pipe 60 and the second shunt pipe 61, respectively. NTU value sensors 58 are fixedly installed on the outside of the first sewage treatment tank 11 and the second sewage treatment tank 12. The two NTU value sensors 58 can provide real-time feedback of the NTU values ​​of the sewage in the first sewage treatment tank 11 and the second sewage treatment tank 12, so as to input the coagulant aid according to the NTU values ​​of the sewage in the first sewage treatment tank 11 and the second sewage treatment tank 12.

[0029] The first and second liquid delivery pipes 14 and 15 are respectively fixedly installed on the outer walls of the first and second sewage treatment tanks 11 and 12, and the second and third liquid delivery pipes 65 and 66 are respectively installed at the bottoms of the first and second sewage treatment tanks 11 and 12, and the second and third liquid delivery pipes 65 and 66 are arranged at lower heights than the first and second liquid delivery pipes 14 and 15. After the coagulant is introduced into the first and second sewage treatment tanks 11 and 12, the coagulant can absorb impurities in the sewage in the first and second sewage treatment tanks 11 and 12, reduce the turbidity of the sewage, increase the sedimentation volume, and shorten the sedimentation time. The first and second liquid delivery pipes 14 and 15 are both connected to the liquid inlet pipeline of the glow cracking sewage treatment equipment, so as to deliver the sewage in the upper layers of the first and second sewage treatment tanks 11 and 12 to the glow cracking sewage treatment equipment. The first liquid delivery pipe 14 and the second liquid delivery pipe 15 are respectively fixedly installed with an eleventh solenoid valve 67 and a twelfth solenoid valve 68, which can be used to control the flow of the first liquid delivery pipe 14 and the second liquid delivery pipe 15. The second drain pipe 65 and the third drain pipe 66 are respectively fixedly installed with a thirteenth solenoid valve 69 and a fourteenth solenoid valve 70 at the liquid outlet ports, so as to discharge the sediment at the bottom of the first sewage treatment tank 11 and the second sewage treatment tank 12.

[0030] The working principle of the present invention is: The sewage generated by the industrial park and enterprises can enter the sedimentation barrel 3 through the water inlet pipe 4. By starting the first motor 23, the rotating rod 20 and the propeller impeller 21 can be rotated together, and under the cooperation of the propeller blade 24, the sewage in the sedimentation barrel 3 is rotated and separated, so that the large particles of impurities in the sewage are precipitated to the bottom of the sedimentation chamber 19, and the sewage in the upper layer of the upper floating chamber 18 can be sent to the separation barrel 7 through the outlet pipe 5. The turbidity sensor 8 can detect the NTU value of the sewage in the separation barrel 7 in real time; if the NTU value of the sewage in the separation barrel 7 is greater than the standard value, the third solenoid valve 33 allows the sewage in the separation barrel 7 to enter the first separation pipe 9 and introduce it into the first sewage treatment tank 11; if the NTU value of the sewage in the separation barrel 7 is less than the standard value, the sewage in the separation barrel 7 is introduced into the second sewage treatment tank 12 through the second liquid delivery pipe 15. The large particles of impurities and sewage at the bottom of the separation barrel 7 can flow into the drainage box 40 through the guide pipe 6, and through the screening effect of the screening box 45, the large particles of impurities are isolated, allowing the sewage to enter the interior of the buffer box 37; the sewage is further precipitated in the buffer box 37, and the small particles of impurities mixed in the sewage are precipitated to the bottom of the buffer box 37, and the upper sewage can be jointly merged into the confluence pipe 53 through the first infusion pipe 49 and the second infusion pipe 50, thereby entering the first sewage treatment tank 11.

[0031] At this time, the NTU value of the sewage in the first sewage treatment tank 11 and the second sewage treatment tank 12 can be fed back in real time through the NTU value sensor 58, so as to cooperate with the ninth solenoid valve 62 and the tenth solenoid valve 63 to further control the flow rate of the coagulant in the first shunt pipe 60 and the second shunt pipe 61, so as to input an appropriate amount of coagulant into the first sewage treatment tank 11 and the second sewage treatment tank 12, so as to perform coagulant treatment on the sewage in the first sewage treatment tank 11 and the second sewage treatment tank 12, promote the condensation of fine particles without edema into flocs, and make them quickly precipitate to the bottom of the first sewage treatment tank 11 and the second sewage treatment tank 12, and make the NTH value of the sewage at the top of the first sewage treatment tank 11 and the second sewage treatment tank 12 within the range specified by the glow cracking sewage treatment equipment, and respectively inject the sewage in the upper layer of the first sewage treatment tank 11 and the second sewage treatment tank 12 into the glow cracking sewage treatment equipment through the first liquid delivery pipe 14 and the second liquid delivery pipe 15, so as to facilitate the glow cracking sewage treatment equipment to perform deep treatment on the sewage.

[0032] In the above-mentioned sewage treatment process, the flow rate of sewage in the water inlet pipe 4 is proportional to the flow rate of sewage in the first liquid delivery pipe 14 and the second liquid delivery pipe 15, and is achieved through the cooperation of the first solenoid valve 28 and the eleventh solenoid valve 67 and the twelfth solenoid valve 68; at the same time, the turbidity sensor 8 and the NTU numerical sensor 58 detect the sewage parameters in real time, so as to facilitate the control of the added volume of the coagulant, make full use of the coagulant ability of the coagulant, avoid injecting too much coagulant into the first sewage treatment tank 11 and the second sewage treatment tank 12, ensure that the wastewater output by the first liquid delivery pipe 14 and the second liquid delivery pipe 15 is not doped with excessive coagulant, and ensure the long-term normal operation of the glow cracking sewage treatment equipment.

[0033] The above description of the disclosed embodiments enables one skilled in the art to implement or use the present invention. Various modifications to these embodiments will be apparent to one skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the present invention. Therefore, the present invention will not be limited to the embodiments shown herein, but rather to the widest scope consistent with the principles and novel features disclosed herein.

Claims

1. A multi-channel drainage device for glow pyrolysis wastewater treatment, comprising a base (1), characterized in that: The pedestal (1) is fixedly mounted with a frame (2), a side of the frame (2) being fixedly provided with a sedimentation barrel (3), the sedimentation barrel (3) being used for preliminarily separating sewage from large particles of impurities, the top of the sedimentation barrel (3) being fixedly connected with an inlet pipe (4) for sewage to enter, the top side wall of the sedimentation barrel (3) being fixedly connected with an outlet pipe (5) for upper sewage to pass through, the bottom of the sedimentation barrel (3) being connected with a flow guide pipe (6), a liquid separation barrel (7) being fixedly mounted on the inner side of the frame (2), the inner cavity of the liquid separation barrel (7) being connected with the outlet pipe (5), a plurality of turbidity sensors (8) being installed in the liquid separation barrel (7), the turbidity sensors (8) being used for detecting the NTU value of sewage in the liquid separation barrel (7), the liquid separation barrel (7) being fixedly connected with a first liquid separation pipe (9) and a second liquid separation pipe (10), the sewage flowing in the first liquid separation pipe (9) The water NTU value is greater than the second liquid dispensing tube (10); the first liquid dispensing tube (9) and the second liquid dispensing tube (10) are respectively connected to a first sewage treatment tank (11) and a second sewage treatment tank (12); the first sewage treatment tank (11) and the second sewage treatment tank (12) are both tightly connected to the pedestal (1); the first sewage treatment tank (11) and the second sewage treatment tank (12) are commonly connected to a coagulant input pipe (13); the coagulant input pipe (13) inputs the coagulant according to the NTU value of the sewage in the first sewage treatment tank (11) and the second sewage treatment tank (12); the first liquid delivery pipe (14) and the second liquid delivery pipe (15) are respectively tightly installed on the outer walls of the first sewage treatment tank (11) and the second sewage treatment tank (12); the first liquid delivery pipe (14) and the second liquid delivery pipe (15) are both connected to the liquid inlet pipeline of the glow cracking sewage treatment equipment.

2. The multi-channel drainage device for glow pyrolysis wastewater treatment according to claim 1 is characterized in that: A first mounting block (16) is fixedly mounted on the side of the frame (2); a second mounting block (17) which is tightly connected to the first mounting block (16) is fixedly mounted on the outer wall of the sedimentation barrel (3); an upper floating chamber (18) and a sedimentation chamber (19) are arranged in the sedimentation barrel (3), the inner diameter of the upper floating chamber (18) is larger than that of the sedimentation chamber (19); the water inlet pipe (4) and the water outlet pipe (5) are both connected to the upper floating chamber (18); the guide pipe (6) is connected to the sedimentation chamber (19); a rotating rod (20) is rotatably arranged in the upper floating chamber (18); a propeller impeller (21) is fixedly mounted on the bottom end of the rotating rod (20); and the propeller impeller (21) is arranged between the upper floating chamber (18) and the sedimentation chamber (19).

3. The multi-channel drainage device for glow pyrolysis wastewater treatment according to claim 2, characterized in that: A base (22) is fixedly mounted on the top of the sedimentation barrel (3), a first motor (23) is fixedly mounted on the base (22), an output shaft of the first motor (23) is drivingly connected to a rotating rod (20), a propeller blade (24) is arranged on the outer side of the rotating rod (20), a plurality of mounting rods (25) are fixedly mounted on the outer wall of the rotating rod (20), each of the mounting rods (25) is provided with a slot (26), a cover cap (27) is fixedly mounted on the outer side of the slot (26), the slot (26) is fastened and clamped to the propeller blade (24), and the rotation radius of the propeller blade (24) is smaller than that of the propeller impeller (21).

4. The multi-channel drainage device for glow pyrolysis wastewater treatment according to claim 1 is characterized in that: A first solenoid valve (28) is installed on the water inlet pipe (4), a second solenoid valve (29) and a first centrifugal pump (30) are installed on the water outlet pipe (5), the bottom of the first centrifugal pump (30) is tightly connected to the pedestal (1), and a second motor (31) is mounted on the top of the first centrifugal pump (30).

5. The multi-channel drainage device for glow pyrolysis wastewater treatment according to claim 1 is characterized in that: A hanging frame (32) is fixedly mounted on the inner top of the frame (2); the bottom of the hanging frame (32) is tightly connected to the outer wall of the liquid dispensing barrel (7); a third solenoid valve (33) and a fourth solenoid valve (34) are respectively mounted on the pipelines of the first liquid dispensing tube (9) and the second liquid dispensing tube (10); a stabilizing frame (35) is fixedly mounted on the pedestal (1); a plurality of pipe seats (36) are fixedly mounted on the top of the stabilizing frame (35); the pipe seats (36) are used to stably arrange the first liquid dispensing tube (9) and the second liquid dispensing tube (10).

6. The multi-channel drainage device for glow pyrolysis wastewater treatment according to claim 1, characterized in that: A buffer box (37) is fixedly mounted on the pedestal (1), an opening (38) is provided at the top of the buffer box (37), a bracket (39) is fixedly mounted on the side of the buffer box (37), a drainage box (40) is fastened to the bracket (39), the drainage box (40) is arranged above the opening (38), a second centrifugal pump (41) and a fifth solenoid valve (42) are installed on the pipeline of the guide pipe (6), a third motor (43) is fixedly mounted on the top of the second centrifugal pump (41), and a liquid outlet port of the guide pipe (6) is arranged vertically downward and arranged above the drainage box (40).

7. The multi-channel drainage device for glow pyrolysis wastewater treatment according to claim 6, characterized in that: A frame (44) is fixedly mounted on the top periphery of the buffer box (37), a screening box (45) is arranged on the inner side of the frame (44), and the screening box (45) is arranged above the opening (38). A slanted portion (46) is arranged on the side of the drainage box (40) close to the opening (38), and the slanted portion (46) is arranged above the screening box (45). A plurality of sieve holes (47) are evenly arranged at the bottom of the sieve box (45), and the passing area of ​​the sieve holes (47) is smaller than that of the opening (38). Handles (48) are fixedly mounted on both sides of the sieve box (45).

8. The multi-channel drainage device for glow pyrolysis wastewater treatment according to claim 6, characterized in that: The side of the buffer box (37) is connected to a first infusion tube (49) and a second infusion tube (50), and a sixth solenoid valve (51) and a seventh solenoid valve (52) are installed on the pipelines of the first infusion tube (49) and the second infusion tube (50), respectively. The first infusion tube (49) and the second infusion tube (50) are connected to a confluence tube (53) together, and a third centrifugal pump (54) is installed on the pipeline of the confluence tube (53). A fourth motor (55) is installed on the top of the third centrifugal pump (54), and the confluence tube (53) is connected to the first sewage treatment tank (11). A first drainage tube (56) is installed at the bottom of the buffer box (37), and the arrangement height of the first drainage tube (56) is lower than that of the first infusion tube (49) and the second infusion tube (50), and an eighth solenoid valve (57) is installed on the pipeline of the first drainage tube (56).

9. The multi-channel drainage device for glow pyrolysis wastewater treatment according to claim 1, characterized in that: An NTU numerical sensor (58) is fixedly installed on the outside of the first sewage treatment tank (11) and the second sewage treatment tank (12); the liquid outlet port of the coagulant input pipe (13) is tightly connected to a three-way pipe (59); the two liquid outlet ports of the three-way pipe (59) are respectively connected to a first shunt pipe (60) and a second shunt pipe (61); a ninth solenoid valve (62) and a tenth solenoid valve (63) are respectively installed on the first shunt pipe (60) and the second shunt pipe (61); the first shunt pipe (60) and the second shunt pipe (61) are respectively connected to the first sewage treatment tank (11) and the second sewage treatment tank (12).

10. The multi-channel drainage device for glow pyrolysis wastewater treatment according to claim 1, characterized in that: Support legs (64) are fixedly mounted on the outer walls of the first sewage treatment tank (11) and the second sewage treatment tank (12); the bottom ends of the support legs (64) are tightly connected to the pedestal (1); a second drainage pipe (65) and a third drainage pipe (66) are respectively mounted on the bottoms of the first sewage treatment tank (11) and the second sewage treatment tank (12); the second drainage pipe (65) and the third drainage pipe (66) are arranged at lower heights than the first liquid delivery pipe (14) and the second liquid delivery pipe (15); an eleventh solenoid valve (67) and a twelfth solenoid valve (68) are respectively fixedly mounted on the first liquid delivery pipe (14) and the second liquid delivery pipe (15); and a thirteenth solenoid valve (69) and a fourteenth solenoid valve (70) are respectively fixedly mounted at the liquid outlet ports of the second drainage pipe (65) and the third drainage pipe (66).

Citation Information

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