A universal rapid clarification and anti-scaling system and its application method

Abstract

The present invention discloses a universal rapid clarification and anti-scaling system and an application method thereof. The system comprises a water inlet pipe with an input pump, the inlet of the water inlet pipe is connected to a water source, the outlet of the water inlet pipe is connected to a pipeline type electric flocculation inlet, the outlet of the pipeline type electric flocculation is connected to a permanent magnet cyclone through a pipeline mixer, the top of the permanent magnet cyclone is connected to a solid-liquid separation device and a pipeline type cyclone separation device through a water pipeline, and the bottom of the permanent magnet cyclone and the solid-liquid separation device are respectively connected to a sediment separation box. The device system of the present invention improves the flocculation treatment effect by adopting the electric flocculation technology combined with a mixer, and utilizes the four-stage enhanced solid-liquid separation technology, with fast and good separation efficiency, small sewage discharge, and no secondary pollution problem. In the long-term operation process, it can effectively avoid common industrial problems such as scaling, wall adhesion, scarring, and blockage, and each component can be used independently or in combination, suitable for various application environments.

Description

Technical Field

[0001] The invention belongs to the field of low-pollution and low-concentration water clarification treatment, and particularly relates to a universal water rapid clarification and anti-scaling system and an application method thereof. Background Art

[0002] In industrial production, such as petrochemical enterprises, steel enterprises, thermal power industry, pesticide and pharmaceutical enterprises, etc., circulating water systems are needed to exchange heat and cool equipment. During the operation of circulating water systems, there are common problems such as heat exchanger scaling, microbial growth, impurity deposition, and water body deterioration. In order to effectively prevent the above problems, the circulating water system generally requires the installation of a bypass filter device in the early stage of construction. In the application of this device, there are problems such as difficulty in backwashing the filter material, compaction of the filter material, large sewage discharge, and high maintenance, which makes the device unable to operate stably for a long time.

[0003] At present, enterprises generally adopt the method of dosing drugs in circulating water to solve the above problems, which also brings about problems such as large discharge volume, adding new pollutants to the water body to form secondary pollution, and continuously increasing treatment costs. In addition, due to the extensive method of adding drugs to the water body, the function of the drugs cannot be fully exerted, resulting in drug waste and excessive pollution. In terms of wastewater dosing treatment, the method of adding drugs and stirring in the dosing barrel is basically adopted. In this way, the drugs and water bodies cannot be fully mixed in the shortest time, which affects the optimal function of the drugs, causing drug loss and excessive addition of drugs, which not only causes economic losses to the company but also causes secondary environmental pollution problems. Summary of the invention

[0004] The present invention provides a universal rapid clarification and anti-scaling system and method for water bodies, which is mainly used in industrial circulating water systems for purifying water bodies and preventing scale, and can also be used in the field of wastewater clarification to eliminate the initial purification of water bodies.

[0005] In order to achieve the above object, the present invention adopts the following technical solutions:

[0006] A universal rapid clarification and anti-scaling system comprises a water inlet pipe with an input pump, wherein the inlet of the water inlet pipe is connected to a water source, the outlet of the water inlet pipe is connected to the inlet of a pipeline electroflocculation, the outlet of the pipeline electroflocculation is connected to a permanent magnet cyclone via a pipeline mixer, the top of the permanent magnet cyclone is connected to a solid-liquid separation device; the solid-liquid separation device comprises a pipeline quasi-static separation device and a pipeline cyclone separator; the bottom of the permanent magnet cyclone and the pipeline quasi-static separation device are respectively connected to a sedimentation separation box.

[0007] Preferably, the pipeline electroflocculation includes a positive electrode, a negative electrode, a power supply and a first transducer; the negative electrode adopts a pipeline shell structure; the power supply is arranged at one end of the negative electrode of the pipeline shell; the positive electrode adopts a dissolving electrode arranged inside the negative electrode pipeline shell, and the negative electrode is provided with a first transducer.

[0008] Preferably, the positive electrode adopts a compound structure, and the positive electrode with a compound structure effectively increases the area of ​​the electrode and improves the electro-flocculation processing capacity.

[0009] Preferably, the permanent magnet cyclone includes a cyclone shell, a yoke is provided in the middle and upper part of the cyclone shell, the yoke includes two upper and lower circular ring structures, the upper and lower circular ring structures are connected by an inner ring, neodymium iron boron permanent magnet material is embedded in the yoke between the two circular ring structures, and small holes are opened in the radial surroundings of the yoke; the centers of the inner rings of the upper and lower circular ring structures of the yoke are connected to a hollow shaft through a bracket, and the hollow shaft is connected to the adjustable speed motor.

[0010] Preferably, the solid-liquid separation device includes a pipeline quasi-static separation device and a pipeline cyclone separation device; the pipeline quasi-static separation device includes a water pipeline and a sediment pipeline and a suspended matter pipeline arranged above and below the water pipeline and parallel to the water pipeline; the water pipeline is connected to the pipeline cyclone separator inlet through a water pipeline valve; the sediment pipeline and the suspended matter pipeline are connected to the water pipeline through a sediment inclined pipe and a suspended matter inclined pipe respectively, and the outlet of the suspended matter pipeline is connected to the sediment separation box through a sediment outlet pipe with a sediment pipeline valve; the outlet of the sediment pipeline is connected to the sediment outlet pipeline through a suspended matter outlet pipe with a suspended matter pipeline valve.

[0011] Preferably, the bottom of the sediment separation box adopts a conical structure, an ultrasonic vibration transmission rod is provided in the sediment separation box, a plurality of groups of separators are serially provided on the ultrasonic vibration transmission rod, and one end of the ultrasonic vibration transmission rod is connected to the sixth transducer outside the sediment separation box.

[0012] Preferably, the pipeline cyclone separation device includes a pipeline shell, a cyclone device is arranged in the pipeline shell, a conical tube wall formed by a plurality of tangential pores is arranged on the tube wall in the middle and lower part of the pipeline shell, a sealed separation chamber is arranged on the outer sleeve of the conical tube wall, a fourth transducer is arranged on the separation chamber, and the bottom of the separation chamber is connected to the input pump inlet on the water outlet pipe through the sediment outlet.

[0013] Preferably, the cyclone device comprises at least one group of guide vanes, and the guide vanes are used to generate a rotating flow of the water flow.

[0014] Preferably, a mixing sheet is provided in the pipeline mixer, and a second transducer is provided on the pipeline mixer.

[0015] Preferably, an iron remover is provided at the front end of the input pump on the water inlet pipe, and the iron remover adopts online cleaning to intercept and remove magnetic substances in the water body.

[0016] The present invention also provides an application method of a universal rapid clarification and anti-scaling system, the steps of which are as follows:

[0017] S1: The water to be treated first passes through the iron remover through the inlet of the water inlet pipe, and then is input into the pipeline electric flocculation through the input pump; the iron remover uses online cleaning to intercept and remove magnetic substances in the water;

[0018] S2: During operation, the negative electrode of the pipeline housing always maintains high-frequency and low-amplitude fluctuations under the ultrasonic wave of the first transducer, which can prevent the problem of dirt sticking to the wall and positive electrode passivation, and effectively polymerize impurities in the water and promote the mixing of flocculants with the water;

[0019] S3: The electroflocculated material preliminarily mixed with the water body enters the pipeline mixer. An ultrasonic second transducer is set outside the pipeline mixer to perform high-frequency microscopic disturbance on the water body in the pipeline mixer; a static mixing sheet is set inside the pipeline mixer to perform macroscopic disturbance on the water body in the pipeline, and the mass transfer, mixing and polymerization of flocculants and impurities in the water body are further promoted under macroscopic and microscopic disturbances;

[0020] S4: The mixed electro-flocculated substances enter the permanent magnetic cyclone. When the adjustable speed top operation is carried out, the fluid can circulate from the center of the magnetic yoke ring structure under the action of centrifugal force, and enter the U-shaped magnetic yoke along the small holes opened radially around the magnetic yoke, and contact with the NdFeB permanent magnet material embedded in the U-shaped magnetic yoke, so that the fluid passes through the magnetic field, preparing for the subsequent solid-liquid separation;

[0021] S5: The clear liquid and flocculated mixture treated by the permanent magnet cyclone are discharged from the cyclone outlet pipe and enter the water pipe of the pipeline quasi-static separation device, and the treated turbid liquid is discharged from the bottom outlet pipe of the permanent magnet cyclone and enters the sediment separation box; during the flow in the water pipe, the gravity sediment and concentrate generated by flocculation gradually enter the sediment pipe through the sediment inclined pipe connected below the water pipe, and the suspended matter generated in the flocculation enters the suspended matter pipe through the suspended matter inclined pipe connected above; the sediment and suspended matter are in a dynamic separation process through the inclined pipe during the separation process; the clear liquid in the water pipe flows forward steadily to the end, and most of the sediment and suspended matter are separated, and enter the inlet of the pipeline cyclone separator after passing through the water pipe valve on the water pipe; the other two sediment pipes and the suspended matter pipe outlets are collected and transported to the bottom of the sediment separation box after passing through the sediment pipe valve and the suspended matter pipe valve, and discharged outward;

[0022] S6: After the clear liquid passes through the water pipe valve and enters the inlet of the pipe cyclone separator, the fluid generates a rotating flow under the action of two sets of guide vanes. Since the flocculated sediment has a higher specific gravity than the water body, it tends to the outer circle under the action of the cyclone and reaches the tangent fine hole. The pipe diameter becomes smaller and the flocculated sediment is discharged from the tangent fine hole. The clear liquid is discharged from the clear water outlet of the center hole, and the turbid liquid is discharged from the sediment outlet and refluxes to the inlet end of the input pump;

[0023] At the same time, the sedimentation fluid discharged from the bottom flow outlet of the permanent magnet cyclone and the sediment pipe and suspended matter pipe of the pipeline quasi-static separation device enters the sedimentation separation box, and the sediment containing water is quickly separated by the inclined tube settler or the horizontal tube settler. The clear liquid floating on the sedimentation separation box is combined with the clear liquid discharged from the pipeline cyclone separator through the upper clear water outlet pipe, and is transported to the inlet of the input pump as reflux liquid for circulation treatment.

[0024] Compared with the prior art, the present invention has the following beneficial effects:

[0025] 1. The present invention adopts ultrasonic pipeline dosing flocculation technology or electric flocculation technology to avoid electrode polarization and passivation problems, which can not only maintain electrolysis efficiency, but also accelerate the mixing and mass transfer of flocculants and water bodies, thereby improving the flocculation treatment effect.

[0026] 2. The present invention adopts external force driven cyclone magnetization technology to further enhance the flocculation treatment effect.

[0027] 3. The present invention adopts three-layer horizontal tube separation technology to quickly separate flocculated sediments and flocculated suspended matter.

[0028] 4. The present invention adopts pipeline cyclone separation device technology to further separate flocculated sediments to ensure that the output clear liquid quality meets the standards.

[0029] 5. The present invention adopts ultrasonic inclined plate or horizontal plate solid-liquid rapid separation technology to further separate the separated flocculated sediment to minimize the water content of the effluent. If it is used in conjunction with a spiral sludge dewatering machine, the liquid is refluxed and the extrudate is treated as dry garbage or solid waste, closed-loop solid-liquid separation can be achieved.

[0030] 6. The device system of the present invention not only has good water purification and clarification functions, but more importantly has anti-scaling and descaling functions. It can ensure that the clear liquid will not scale in subsequent pipelines and heat exchangers; for equipment that has already scaled, the old scale will gradually fall off.

[0031] 7. The device system of the present invention is mainly composed of pipelines, which occupies a small area and has a large processing capacity per unit volume; each component can be used independently or in combination, and it is easy to implement standardized and modular production and application, and is suitable for various application environments.

[0032] 8. The system of the device of the present invention is easy to expand. Small capacity expansion can be effectively solved by lengthening the length of the pipeline mixer and the horizontal pipe separator pipeline; medium capacity expansion can be effectively solved by increasing the diameter of the pipeline mixer and the horizontal pipe separator pipeline; large capacity expansion can be effectively solved by paralleling the device system.

[0033] 9. The device system of the present invention adopts a four-stage enhanced solid-liquid separation technology, which has fast separation efficiency, good separation effect, small sewage discharge, no secondary pollution problem, strong load impact resistance, and no clogging problem of filtering technology.

[0034] 10. The device system of the present invention can effectively avoid common industrial problems such as scaling, wall sticking, scarring, and blockage during long-term operation, and can completely reach a maintenance-free state. Combined with full-automatic control technology, it can realize a truly unattended processing system.

[0035] 11. The device system of the present invention is a universal purification and separation system, which can be used not only in the field of circulating water purification, but also in the field of wastewater treatment and industrial process. In short, the device system is an efficient pipeline reactor that can effectively replace the traditional dosing box and reactor system.

[0036] In summary, the device system of the present invention improves the flocculation treatment effect by adopting the electric flocculation technology, improves the flocculation treatment effect by combining the mixer, and utilizes the four-stage enhanced solid-liquid separation technology, with fast separation efficiency, good separation effect, small discharge volume, no secondary pollution problem, strong load impact resistance, and no clogging problem of filtering technology. In the long-term operation process, it can effectively avoid common industrial problems such as scaling, wall adhesion, scarring, and clogging. Moreover, each component can be used independently or in combination, and it is easy to implement standardized and modular production and application, which is suitable for various application environments. BRIEF DESCRIPTION OF THE DRAWINGS

[0037] Figure 1 A schematic diagram of the structure of a universal rapid clarification and anti-scaling system proposed by the present invention;

[0038] Figure 2 A schematic diagram of the structure of a permanent magnet cyclone in a general rapid clarification and anti-scaling system proposed by the present invention;

[0039] Figure 3 A schematic diagram of the structure of a horizontal tube and an inclined tube device in a universal rapid clarification and anti-scaling system proposed by the present invention;

[0040] Figure 4 This is a schematic diagram of the tangent pore structure of a pipeline cyclone separator in a universal rapid clarification and anti-scaling system proposed by the present invention.

[0041] Numbers in the figure:

[0042] 1. Pipeline electroflocculation; 1.1. Positive electrode; 1.2. Negative electrode; 1.3. Power supply; 2. First transducer; 3. Iron remover; 4. Input pump; 5. Pipeline mixer; 6. Mixing sheet; 7. Second transducer; 8. Permanent magnet cyclone; 8.1. Cyclone housing; 8.2. Magnetic yoke; 8.3. NdFeB permanent magnet material; 8.4. Small hole; 8.5. Adjustable speed motor; 8.6. Hollow shaft; 9. Water pipeline; 10. Sediment pipeline; 11. Suspended matter pipeline; 12. Suspended matter inclined tube; 13. Third transducer; 14. Sediment inclined tube pipe; 15, suspended matter pipe valve; 16, suspended matter outlet pipe; 17, water pipe valve; 18, pipe cyclone separator; 18.1, guide vane; 18.2, separation chamber; tangential pore 18.3; 18.4, clean water outlet; 18.5, sediment outlet; 19, fourth transducer; 20, sediment outlet pipe; 21, sediment pipe valve; 22, sediment separation box; 22.1, separator; 22.2, ultrasonic transmission rod; 22.3, upper clean water outlet pipe; 23, fifth transducer; 24, sixth transducer. DETAILED DESCRIPTION

[0043] The technical solutions in the embodiments of the present invention will be described clearly and completely below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, rather than all the embodiments.

[0044] like Figure 1 As shown, a universal rapid clarification and anti-scaling system provided by the present invention, the device system includes a flocculant generating part, a mixing part, an enhanced polymerization part, a solid-liquid separation part, a sediment concentration part and a seed reflux part, namely, a pipeline electroflocculation 1, a pipeline mixer 5, a permanent magnet cyclone 8, a pipeline quasi-static separation device and a pipeline cyclone separation device 18, a sediment separation box 22 and a seed reflux part.

[0045] The flocculant generation part used in the present invention is composed of a pipeline reactor, which can be used to generate flocculants by electric flocculation or by adding drugs.

[0046] The electro-flocculation method produces floccules: the positive electrode of the electro-flocculation is set in a metal pipe, and the material of iron or aluminum is selected according to the characteristics of the treated water body. The negative electrode of the electro-flocculation is common to the pipe, and an ultrasonic transducer is set outside the pipe. The ultrasonic control power supply and the electro-flocculation power supply are set nearby. The characteristics of this device are: first, it can effectively avoid the problems of electrode polarization and electrode passivation and electrolysis efficiency generated during the operation of the electro-flocculation device; second, it can make the flocculent material produced by electrolysis and the impurities in the water body quickly mix, and its mass transfer efficiency is more than 20 times higher than that of ordinary electro-flocculation devices, thereby achieving a better treatment effect. (The pipeline electro-flocculation 1 adopted by the present invention is the electro-flocculation method to produce floccules)

[0047] The method of producing floccules by adding medicine: a dosing port is set at the front end of the metal pipe, a static mixing spoiler is set inside the pipe, an ultrasonic transducer is set outside the pipe, and an ultrasonic control power supply and a dosing device are set nearby. After the liquid medicine enters the pipe, it is quickly mixed within 1 second under the action of ultrasound and spoilers, avoiding the problem of waste caused by hydrolysis of medicines that cannot be mixed quickly. Compared with ordinary dosing devices, the same effect can be achieved by reducing the amount of medicine added by more than 15% when treating the same water body.

[0048] Whether it is the floccules produced by electro-flocculation or by adding drugs, the floccules can be quickly mixed with the water body, and the concentration difference diffusion further promotes the mass transfer effect, which is a microscopic effect; in addition, the water body in the pipeline reactor flows in a piston-like water column, and the water body is updated quickly. From a macroscopic perspective, the mixing of floccules and water is more uniform, and there is no problem of mixing dead corners and repeated mixing due to drug addition. The above two technical results fully ensure the application effect of the device of the present invention.

[0049] The mixing part is set after the flocculant generation part. Its purpose is to further mix the flocculants generated in the front with the water body through mass transfer, and to make preliminary preparations for giving full play to the functions of compression double electric layer, adsorption electric neutralization, adsorption bridge, and precipitation net capture between flocculants and impurities in the water body. This part is composed of a static mixing sheet built into the metal pipe and an ultrasonic transducer set outside the pipe. The mixing effect is more than 15 times higher than that of ordinary cylinder stirring pipe mixers.

[0050] The enhanced polymerization part is arranged after the mixing part. The present invention adopts a permanent magnetic cyclone device. The shell of the device is a cyclone structure, and a rotor permanent magnetic pole that can be driven by an external force is arranged inside.

[0051] The pipeline quasi-static separation device is composed of three layers of horizontal pipes and several inclined pipes, and the angle between the inclined pipes and the horizontal is between 30 degrees and 85 degrees. The water body and the flocculation mixture coming out of the enhanced polymerization device enter the middle horizontal pipe. During the flow process, the gravity sediment and concentrate produced by flocculation gradually enter the lowest horizontal pipe through the lower inclined pipe, and the suspended matter produced in the flocculation enters the uppermost horizontal pipe through the upper inclined pipe. Sediment and suspended matter are in a dynamic separation process through the inclined pipe during the separation process. In order to further improve the separation effect, horizontal inclined plates can be set in the horizontal pipes and the inclined pipes. Ultrasonic transducers are set on the middle horizontal pipe, so that the horizontal and inclined pipes can generate high-frequency compression functions during operation, which can further aggregate impurities in the water body and avoid scaling problems in the pipes.

[0052] The pipeline cyclone separation device is set at the outlet of the middle horizontal pipe. It consists of two parts: one is the cyclone device inside the pipe, which is used to convert the incoming liquid into a cyclone state; the other is the tangent hole on the pipe wall, where the pipe wall is conical, and a sealing barrel is set outside it. The fourth ultrasonic transducer is also set on the sealing barrel to prevent the hole from being blocked and accelerate separation. The clear liquid flows out from the tangent hole and is finally discharged through the clean water outlet pipe on the shell. The turbid liquid flows out from the lower end of the pipe and enters the inlet of the input pump.

[0053] The sediment concentration and seed reflux device, the sediment fluid discharged by the enhanced polymerization and solid-liquid separation device enters the sediment concentration part, and the sediment containing water is quickly separated through the inclined tube or horizontal tube. The floating clear liquid can directly merge with the clear liquid discharged by the pipeline cyclone separation device, or it can be transported to the inlet of the input pump as a reflux liquid for reprocessing. The reflux liquid contains a large amount of seed crystals, which has a good effect on the subsequent purification and scale prevention of water bodies. The seed crystals are the products of flocculation crystallization polymerization, ultrasonic polymerization and magnetization polymerization in the device system. In order to achieve the initial solid-liquid separation, ultrasonic energy is added to the inclined plate or horizontal plate, which can quickly aggregate the particles near the plate wall and accelerate sedimentation; in order to smoothly discharge the sediment on the wall of the hopper at the bottom of the sediment separation box, an ultrasonic transducer is set on the outer wall to prevent the occurrence of wall adhesion when discharging sediment. In addition, in order to further accelerate the sedimentation rate of the sediment, a positively charged electrode plate can be set inside the hopper to adsorb negatively charged flocculated sediment. Example

[0054] Specifically, it includes a water inlet pipe with an input pump 4, the inlet of the water inlet pipe is connected to a water source, the outlet of the water inlet pipe is connected to the inlet of a pipeline electroflocculation 1, the pipeline electroflocculation 1 includes a positive electrode 1.1, a negative electrode 1.2, a power supply 1.3 and a first transducer 2; the negative electrode 1.2 adopts a pipeline shell structure; the power supply 1.3 is arranged at one end of the negative electrode 1.2 of the pipeline shell; the positive electrode 1.1 adopts a dissolving electrode arranged inside the pipeline shell of the negative electrode 1.2, and the negative electrode 1.2 is provided with a first transducer 2.

[0055] Furthermore, aluminum or iron can be used according to the characteristics of the treated water. The power supply 1.3 must be a safe voltage below 36V, the current is determined by the electrode area, the voltage and current are controllable, and can be either direct current or square wave. The positive electrode 1.1 can be a single-stage, only set inside the negative electrode 1.2, or it can be a multiple-stage, that is, another circle is set outside the negative electrode 1.2, and another layer of negative electrode is added. This can effectively increase the area of ​​the electrode and improve the electro-flocculation treatment capacity.

[0056] The outlet of the pipeline electroflocculation 1 is connected to the permanent magnet cyclone 8 through the pipeline mixer 5, and the top of the permanent magnet cyclone 8 is connected to the solid-liquid separation device; the solid-liquid separation device includes a pipeline quasi-static separation device and a pipeline cyclone separator 18; the bottom of the permanent magnet cyclone 8 and the pipeline quasi-static separation device are respectively connected to the sedimentation separation box 22.

[0057] Furthermore, a mixing sheet 6 is provided in the pipeline mixer 5, and a second transducer 7 is provided on the pipeline mixer 5. The water in the pipeline is subjected to high-frequency microscopic disturbance through the second transducer 7, and the water in the pipeline is subjected to macroscopic disturbance through the mixing sheet 6, so that mass transfer, mixing and aggregation of flocculants and impurities in the water are further promoted under macroscopic and microscopic disturbances.

[0058] like Figure 2As shown, the permanent magnet cyclone 8 provided by the present invention includes a cyclone housing 8.1, and a yoke 8.2 is provided in the middle and upper part of the cyclone housing 8.1. The yoke 8.2 includes two upper and lower circular ring structures, and the upper and lower circular ring structures are connected by an inner ring. The yoke 8.2 between the two circular ring structures is embedded with a neodymium iron boron permanent magnet material 8.3. From a top view, the yoke 8.2 is a circular ring structure as a whole, and from a horizontal view, the side of the yoke 8.2 is a U-shaped inner concave structure; small holes 8.4 are opened around the radial sides of the yoke 8.2, and the yoke 8.2 can be single-layer or multi-layer, which is determined by the size and processing capacity of the cyclone housing 8.1. The inner ring centers of the upper and lower circular ring structures of the yoke 8.2 are connected to a hollow shaft 8.6 through a bracket, and the hollow shaft 8.6 is connected to an adjustable speed motor 8.5; when the adjustable speed top 8.5 is in operation, the fluid can pass through the magnetic field in the U-shaped yoke 8.2 from the center of the yoke 8.2 under the action of centrifugal force. The device can effectively control the magnetization intensity of water. The following effects can be obtained when the water and flocculants are treated by the device:

[0059] First, it will have a certain impact on the physical and chemical properties of water. After magnetization, the physical and chemical properties of water, such as activity, surface tension, hydrogen bond angle, and solubility, will undergo significant changes.

[0060] Secondly, it is beneficial to weaken the double electric layer of charged particles, reduce the repulsive force of colloidal particles, increase the Zeta potential of particles, promote the rate of floc collision and aggregation to form larger and more stable flocs, and further promote the coagulation and flocculation effects;

[0061] Third, the particle size distribution range of the magnetized flocs becomes narrower, the particle size distribution tends to be more concentrated, and the floc structure becomes more regular.

[0062] Prepare for the subsequent solid-liquid separation.

[0063] The pipeline type quasi-static separation device comprises three layers of horizontal pipes and a plurality of inclined pipes, wherein the three layers of horizontal pipes comprise a water pipe 9 and a sediment pipe 10 and a suspended matter pipe 11 arranged above and below the water pipe 9 and parallel to each other; the water pipe 9 is connected to the inlet of the pipeline cyclone separator 18 through a water pipe valve 17; the plurality of inclined pipes comprise a plurality of sediment inclined pipes 14 and a plurality of suspended matter inclined pipes 12; the sediment pipe 10 and the suspended matter pipe 11 are connected to the water pipe 9 through a plurality of sediment inclined pipes 14 and a plurality of suspended matter inclined pipes 12 respectively, the outlet of the suspended matter pipe 11 is connected to the sediment separation box 22 through a sediment outlet pipe 20 with a sediment pipe valve 21; the outlet of the sediment pipe 10 is connected to the sediment outlet pipe 20 through a suspended matter outlet pipe 16 with a suspended matter induction valve 15. By controlling the opening of the suspended matter pipe valve 15, the water pipe valve 17 and the sediment pipe valve 21, the flow of the clear liquid and the turbid liquid can be reasonably controlled to achieve the best separation effect.

[0064] Further, the distance between adjacent inclined tubes in the plurality of sediment inclined tubes 14 and the plurality of suspended material inclined tubes 12 is defined to be between 200 mm and 500 mm. Figure 3 As shown, the angle between the inclined pipe and its corresponding horizontal pipe (i.e., the sediment pipe 10 or the suspended matter pipe 11) is between 30 degrees and 85 degrees, the length of the suspended matter inclined pipe 12 is set between 300 mm and 500 mm, the length of the sediment inclined pipe 14 is set between 400 mm and 800 mm, the inner diameter of the horizontal pipe is set between 100 mm and 250 mm, and the length of the horizontal pipe is set between 1000 mm and 10000 mm. The specific values ​​are determined by the processing volume and processing standards, and the pipes are all made of metal.

[0065] In order to further improve the separation effect, a third transducer 13 is arranged on the water pipe 9, so that the three-layer horizontal pipe and inclined pipe can generate a high-frequency compression function during operation, which can further aggregate impurities in the water body and avoid scaling problems in the pipe.

[0066] The pipeline cyclone separation device 18 comprises a pipeline housing, the bottom of which is a clean water outlet 18.4 for discharge; two sets of guide vanes 18.2 are arranged in the pipeline housing to generate a rotating flow of water. Figure 4 As shown, a conical tube wall formed by a plurality of tangential fine holes 18.3 is provided on the tube wall in the middle and lower part of the pipeline-type housing, and a sealed separation chamber 18.2 is provided on the outer sleeve of the conical tube wall. A fourth transducer 19 is provided on the separation chamber 18.2 to prevent the tangential fine holes from being blocked and to accelerate the separation of the clear liquid; the bottom of the separation chamber 18.2 is connected to the inlet of the input pump 4 on the outlet pipe through the sediment outlet 18.5.

[0067] An ultrasonic transmission rod 22.2 is provided in the sediment separation box 22, and a plurality of groups of separators 22.1 are connected in series on the ultrasonic transmission rod 22.2, and one end of the ultrasonic transmission rod 22.2 is connected to the sixth transducer 24 outside the sediment separation box 22. The ultrasonic transmission rod 22.2 is driven by the sixth transducer 24 to transmit ultrasonic waves to each separator 22.1 on the ultrasonic transmission rod 22.2, which can quickly remove particles near the separator 22.1 and accelerate sedimentation; in order to discharge sediment smoothly, the bottom of the sediment separation box 22 adopts a cone structure, and the outer side of the bottom of the cone is provided with a fifth transducer 23 to prevent the occurrence of wall adhesion when discharging sediment. In addition, in order to further accelerate the sedimentation speed of the sediment, a positively charged electrode plate can be set inside the cone to adsorb negatively charged flocculated sediment.

[0068] Furthermore, the sediment separation box 22 is connected to the inlet of the input pump 4 on the water inlet pipe through the upper clear water outlet pipe 22.3 for reflux. The reflux liquid contains a large amount of crystal seeds, which have a good effect on the subsequent purification and scale prevention of the water body. The crystal seeds are the products of flocculation crystallization polymerization, ultrasonic polymerization and magnetization polymerization in the device system.

[0069] Furthermore, an iron remover 3 is provided at the front end of the input pump 4 on the water inlet pipe. The iron remover 3 adopts online cleaning to intercept and remove magnetic substances in the water body.

[0070] The present invention also provides an application method of a universal rapid clarification and anti-scaling system, the steps of which are as follows:

[0071] S1: The water to be treated first passes through the iron remover 3 through the inlet of the water inlet pipe, and then is input into the pipeline electro-flocculation 1 through the input pump 4; wherein, the iron remover 3 uses online cleaning to intercept and remove magnetic substances in the water.

[0072] S2: During operation, the negative electrode 1.2 of the pipeline shell always maintains high-frequency and low-amplitude fluctuations under the ultrasonic wave of the first transducer 2. First, it can prevent the problem of dirt sticking to the wall; second, it can prevent the problem of positive electrode passivation; third, it can effectively aggregate impurities in the water body; and fourth, it can promote the mixing of flocculants and water.

[0073] S3: The electro-flocculated material preliminarily mixed with the water body enters the pipeline mixer 5. Since the ultrasonic second transducer 7 is arranged outside the pipeline mixer 5, the water body in the pipeline mixer 5 is subjected to high-frequency microscopic disturbance. The static mixing sheet 6 is arranged inside the pipeline mixer 5 to perform macroscopic disturbance on the water body in the pipeline, and the mass transfer, mixing and polymerization of flocculants and impurities in the water body are further promoted under the macroscopic and microscopic disturbances.

[0074] S4: The mixed electro-flocculated material enters the permanent magnetic cyclone 8. When the adjustable speed top 8.5 is in operation, the fluid can circulate from the center of the circular structure of the yoke 8.2 under the action of centrifugal force, and enter the U-shaped yoke 8.2 along the small holes 8.4 radially opened on the yoke 8.2, and contact with the NdFeB permanent magnet material 8.3 embedded in the U-shaped yoke 8.2, so that the fluid passes through the magnetic field, preparing for the subsequent solid-liquid separation.

[0075] S5: The clear liquid and flocculated mixture treated by the permanent magnet cyclone 8 are discharged from the cyclone outlet pipe into the water pipe 9 of the pipeline quasi-static separation device, and the treated turbid liquid is discharged from the bottom outlet pipe of the permanent magnet cyclone 8 into the sediment separation box 22; during the flow in the water pipe 9, the gravity sediment and concentrate produced by flocculation gradually enter the sediment pipe 10 through the sediment inclined pipe 14 connected below the water pipe 9, and the suspended matter produced in the flocculation enters the suspended matter pipe 11 through the suspended matter inclined pipe 12 connected above. Sediments and suspended matter are in a dynamic separation process through the inclined pipe during the separation process. The clear liquid in the water pipe 9 flows forward steadily to the end, and most of the sediments and suspended matter are separated, and enter the inlet of the pipeline cyclone separator 18 after passing through the water pipe valve 17 on the water pipe 9. The other two sediment pipes 10 and the suspended matter pipe 11 outlets are collected and transported to the bottom of the sediment separation box 22 after passing through the sediment pipe valve 21 and the suspended matter pipe valve 15.

[0076] S6: After the clear liquid passes through the water pipe valve 17 and enters the inlet of the pipe cyclone separator 18, the fluid generates a rotating flow under the action of the two sets of guide plates 18.1. Since the flocculated sediment has a greater specific gravity than the water body, it tends to the outer circle under the action of the cyclone and reaches the tangent fine hole 18.3. The pipe diameter becomes smaller, and the flocculated sediment is discharged from the tangent fine hole 18.3. The clear liquid is discharged from the clear water outlet 18.4 of the central hole, and the turbid liquid is discharged from the sediment outlet 18.5 and refluxes to the inlet end of the input pump 4.

[0077] At the same time, the sediment fluid discharged from the bottom flow outlet of the permanent magnet cyclone 8 and the sediment pipeline 10 and the suspended matter pipeline 11 of the pipeline quasi-static separation device enters the sediment separation box 22, and the sediment containing water is quickly separated by the inclined tube settler or the horizontal tube settler. The clear liquid floating in the sediment separation box 22 can be directly merged with the clear liquid discharged from the pipeline cyclone separator 18 through the upper clear water outlet pipe 22.3, and can also be transported to the inlet of the input pump 4 as reflux liquid for reprocessing.

[0078] The device system of the present invention adopts the electric flocculation technology to improve the flocculation treatment effect, combines the mixer to improve the flocculation treatment effect, and utilizes the four-stage enhanced solid-liquid separation technology. The separation efficiency is fast, the separation effect is good, the discharge volume is small, there is no secondary pollution problem, the load impact resistance is strong, and there is no clogging problem of the filtering technology. In the long-term operation process, it can effectively avoid common industrial problems such as scaling, wall adhesion, scarring, and clogging. Moreover, each component can be used independently or in combination, and it is easy to implement standardized and modular production and application, which is suitable for various application environments.

[0079] In the description of the present invention, it is to be understood that the terms “center”, “longitudinal”, “lateral”, “length”, “width”, “thickness”, “up”, “down”, “front”, “back”, “left”, “right”, “vertical”, “horizontal”, “top”, “bottom”, “inside”, “outside”, “clockwise”, “counterclockwise”, etc., indicating orientations or positional relationships based on the orientations or positional relationships shown in the accompanying drawings, are only for the convenience of describing the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore should not be understood as a limitation on the present invention.

[0080] In addition, the terms "first" and "second" are used for descriptive purposes only and should not be understood as indicating or implying relative importance or implicitly indicating the number of the indicated technical features. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of the features. In the description of the present invention, the meaning of "plurality" is two or more, unless otherwise clearly and specifically defined.

[0081] The above description is only a preferred specific implementation manner of the present invention, but the protection scope of the present invention is not limited thereto. Any technician familiar with the technical field can make equivalent replacements or changes according to the technical scheme and inventive concept of the present invention within the technical scope disclosed by the present invention, which should be covered by the protection scope of the present invention.

Claims

1. A universal rapid clarification and anti-scaling system, characterized in that: It comprises a water inlet pipe with an input pump (4), the inlet of the water inlet pipe is connected to a water source, the outlet of the water inlet pipe is connected to the inlet of a pipeline type electroflocculation (1), the outlet of the pipeline type electroflocculation (1) is connected to a permanent magnetic cyclone (8) via a pipeline mixer (5), the top of the permanent magnetic cyclone (8) is connected to a solid-liquid separation device; the solid-liquid separation device comprises a pipeline type quasi-static separation device and a pipeline cyclone separator (18); the bottom of the permanent magnetic cyclone (8) and the pipeline type quasi-static separation device are respectively connected to a sediment separation box (22); The pipeline electroflocculation (1) comprises a positive electrode (1.1), a negative electrode (1.2), a power source (1.3) and a first transducer (2); the negative electrode (1.2) adopts a pipeline shell structure; the power source (1.3) is arranged at one end of the negative electrode (1.2) of the pipeline shell; the positive electrode (1.1) adopts a dissolving electrode and is arranged inside the pipeline shell of the negative electrode (1.2); the negative electrode (1.2) is provided with a first transducer (2); The positive electrode (1.1) adopts a compound structure, and the compound structure of the positive electrode (1.1) effectively increases the area of ​​the electrode and improves the electro-flocculation processing capacity; The solid-liquid separation device comprises a pipeline-type quasi-static separation device and a pipeline-type cyclone separation device (18); the pipeline-type quasi-static separation device comprises a water pipeline (9) and a sediment pipeline (10) and a suspended matter pipeline (11) arranged above and below the water pipeline (9) and parallel to the water pipeline (9); the water pipeline (9) is connected to the inlet of the pipeline cyclone separator 18 through a water pipeline valve (17); the sediment pipeline (10) and the suspended matter pipeline (11) are connected to the water pipeline (9) through a sediment inclined pipe (14) and a suspended matter inclined pipe (12) respectively; the outlet of the suspended matter pipeline (11) is connected to a sediment separation box (22) through a sediment outlet pipeline (20) with a sediment pipeline valve (21); the outlet of the sediment pipeline (10) is connected to the sediment outlet pipeline (20) through a suspended matter outlet pipeline (16) with a suspended matter pipeline valve (15).

2. A universal rapid clarification and anti-scaling system according to claim 1, characterized in that: The permanent magnet cyclone (8) comprises a cyclone housing (8.1), a yoke (8.2) is provided in the middle and upper part of the cyclone housing (8.1), the yoke (8.2) comprises two upper and lower circular ring structures, the upper and lower circular ring structures are connected via an inner ring, a neodymium iron boron permanent magnet material (8.3) is embedded in the yoke (8.2) between the two circular ring structures, and small holes (8.4) are provided around the radial direction of the yoke (8.2); the inner ring centers of the upper and lower circular ring structures of the yoke (8.2) are connected to a hollow shaft (8.6) via a bracket, and the hollow shaft (8.6) is connected to an adjustable speed motor (8.5).

3. A universal rapid clarification and anti-scaling system according to claim 2, characterized in that: The bottom of the sediment separation box (22) adopts a conical structure. An ultrasonic vibration transmission rod (22.2) is provided in the sediment separation box (22). A plurality of groups of separators (22.1) are provided in series on the ultrasonic vibration transmission rod (22.2). One end of the ultrasonic vibration transmission rod (22.2) is connected to a sixth transducer (24) outside the sediment separation box (22).

4. A universal rapid clarification and anti-scaling system according to claim 3, characterized in that: The pipeline cyclone separation device (18) comprises a pipeline housing, a cyclone device is arranged in the pipeline housing, and the cyclone device is used to generate a rotating flow in water; a conical tube wall formed by a plurality of tangential pores (18.3) is arranged on the tube wall in the middle and lower part of the pipeline housing, a sealed separation chamber (18.2) is arranged on the outer sleeve of the conical tube wall, a fourth transducer (19) is arranged on the separation chamber (18.2), and the bottom of the separation chamber (18.2) is connected to the inlet of the input pump (4) on the outlet pipe through the sediment outlet (18.5).

5. A universal rapid clarification and anti-scaling system according to claim 4, characterized in that: A mixing sheet (6) is provided in the pipeline mixer (5), and a second transducer (7) is provided on the pipeline mixer (5).

6. A universal rapid clarification and anti-scaling system according to claim 5, characterized in that: An iron remover (3) is provided at the front end of the input pump (4) on the water inlet pipe. The iron remover (3) adopts online cleaning to intercept and remove magnetic substances in the water body.

7. The method for using a universal rapid clarification and anti-scaling system according to claim 6, characterized in that: Here are the steps: S1: The water to be treated first passes through the iron remover (3) through the inlet of the water inlet pipe, and then is input into the pipeline electroflocculation (1) through the input pump (4); the iron remover (3) uses online cleaning to intercept and remove magnetic substances in the water; S2: During operation, the negative electrode (1.2) of the pipeline housing always maintains high-frequency and low-amplitude fluctuations under the ultrasonic wave of the first transducer (2), which can prevent the problem of dirt adhering to the wall and positive electrode passivation, and effectively aggregate impurities in the water body and promote the mixing of flocculants with the water body; S3: The electro-flocculated material that is initially mixed with the water body enters the pipeline mixer (5), and an ultrasonic second transducer (7) is arranged outside the pipeline mixer (5) to perform high-frequency microscopic disturbance on the water body in the pipeline mixer (5); a static mixing sheet (6) is arranged inside the pipeline mixer (5) to perform macroscopic disturbance on the water body in the pipeline, and the mass transfer, mixing and aggregation of flocculants and impurities in the water body are further promoted under the macroscopic and microscopic disturbances; S4: The mixed electro-flocculated material enters the permanent magnetic cyclone (8). When the adjustable speed top (8.5) is in operation, the fluid can circulate from the center of the circular ring structure of the magnetic yoke (8.2) under the action of centrifugal force, and enter the U-shaped magnetic yoke (8.2) along the small holes (8.4) opened radially around the magnetic yoke (8.2), and contact with the neodymium iron boron permanent magnet material (8.3) embedded in the U-shaped magnetic yoke (8.2), so that the fluid passes through the magnetic field, preparing for the subsequent solid-liquid separation; S5: The clear liquid and flocculated mixture treated by the permanent magnetic cyclone (8) are discharged from the cyclone outlet pipe into the water pipe (9) of the pipeline-type quasi-static separation device, and the treated turbid liquid is discharged from the bottom outlet pipe of the permanent magnetic cyclone (8) into the sediment separation box (22); during the flow in the water pipe (9), the gravity sediment and concentrate generated by flocculation gradually enter the sediment pipe (10) through the sediment inclined pipe 14 connected below the water pipe (9), and the suspended matter generated during the flocculation enters the suspended matter inclined pipe (12) connected above. The sediment and suspended matter are in a dynamic separation process through the inclined tube during the separation process; the clear liquid in the water pipe (9) flows smoothly forward to the end, and most of the sediment and suspended matter are separated, and enter the inlet of the pipe cyclone separator (18) after passing through the water pipe valve (17) on the water pipe (9); the outlets of the other two sediment pipes (10) and the suspended matter pipe (11) are collected and transported to the bottom of the sediment separation box (22) after passing through the sediment pipe valve (21) and the suspended matter pipe valve (15), and discharged outward; S6: After the clear liquid passes through the water pipe valve (17) and enters the inlet of the pipe cyclone separator (18), the fluid generates a rotating flow under the action of the two sets of guide plates (18.1). Since the flocculated sediment has a greater specific gravity than the water body, it tends to the outer circle under the action of the cyclone and reaches the tangent fine hole (18.3). The pipe diameter becomes smaller and the flocculated sediment is discharged from the tangent fine hole (18.3). The clear liquid is discharged from the clear water outlet (18.4) of the central hole, and the turbid liquid is discharged from the sediment outlet (18.5) and flows back to the inlet end of the input pump (4); At the same time, the sediment fluid discharged from the bottom flow outlet of the permanent magnet cyclone (8) and the sediment pipe (10) and the suspended matter pipe (11) of the pipeline quasi-static separation device enters the interior of the sediment separation box (22), and the sediment containing water is quickly separated by the inclined tube settler or the horizontal tube settler. The clear liquid floating on the sediment separation box (22) is combined with the clear liquid discharged from the pipeline cyclone separator (18) through the upper clear water outlet pipe (22.3) and is transported to the inlet of the input pump (4) as reflux liquid for circulation treatment.

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