Pyramid type green energy environmental control fluid treatment system

Abstract

The utility model provides a pyramid type green energy environmental control fluid treatment system. The pyramid type green energy environmental control fluid treatment system comprises a green energy environmental control fluid processor module arranged in a diversion channel system. The green energy environment control fluid processor module is a washing module or a demisting module. The washing module comprises a plurality of washing grids which are attached and stacked, and the front face and the back face of each washing grid are concavely provided with a first front face pyramid-shaped washing groove and a first back face pyramid-shaped washing groove which are distributed in an array mode respectively. The wall surface of each first front pyramid-shaped washing tank and the wall surface of each first back pyramid-shaped washing tank are respectively provided with a first front hollow washing hole and a first back hollow washing hole; the structure of the monofilament three-dimensional pyramid-shaped stacked woven layer has directivity, so that the monofilaments are almost perpendicular to the airflow direction, fluid to be treated can be effectively separated from gas-phase fluid to remove mist liquid drops in the airflow, and small and small fog drops in the airflow can be more easily collided to form large fog drops due to the tower-shaped structure. Therefore, the efficiency of treating the polluted fluid is effectively improved.

Description

Technical Field

[0001] The utility model relates to the technical field of polluted fluid treatment, and particularly relates to a pyramid-type green energy environmental control fluid treatment system. Background Art

[0002] In industrial fields such as the semiconductor and panel industries, petrochemical industries, printing and dyeing-related industries, electronics, printed circuit board manufacturing, pulp, paper-related industries, chemical pesticide production-related industries, sulfuric acid manufacturing, chlor-alkali production, steel, metallurgy fields, electroplating processes, surface processing industries, and wastewater treatment, a large amount of industrial waste gas will be generated during the production process. This industrial waste gas contains various pollutants; in particular, it is difficult to remove fine pollution particles, acid mist, aerosol, etc., resulting in environmental pollution and endangering the physical health of workers and nearby residents near the environment. Secondly, in terms of atmospheric emissions, the national emission requirements are becoming increasingly strict. The desulfurization and acid mist removal devices currently used by petrochemical and chemical enterprises are outdated, and there is generally a situation where the discharged acid mist fails to meet the standards, and there is even a serious problem of white smoke emissions. Up to now, the well-known method for acid mist removal devices is to use a desulfurization treatment method, whose main function is to desulfurize and treat tail gas. Since the tail gas after desulfurization treatment cannot meet the specified emission standards, further washing treatment must be carried out to remove acid mist, thus causing inconvenience and trouble during the washing acid mist treatment.

[0003] To improve the above deficiencies, most of the devices most commonly used by those in the relevant technical fields are a kind of washing equipment of a demister, which is generally installed near the outlet area of the equipment to minimize air pollution to the greatest extent; however, due to the non-directional structure of the demister in the relevant technology, the washing fabric is less likely to be perpendicular to the air flow direction, resulting in poor effect of removing fog droplets in the air flow, and thus it is less likely to improve the washing and demisting efficiency. And it has no structural settings of functional materials such as catalyst, hydrophobic, and antibacterial, so it is impossible to effectively reduce the pressure loss and reduce the blockage of the washer by the mildew inhibition effect. Summary of the Utility Model

[0004] The utility model aims to solve at least one of the technical problems in the above technologies to a certain extent.

[0005] To this end, the first object of the present utility model is to provide a pyramid-shaped green energy environmental control fluid treatment system, which mainly consists of a three-dimensional pyramid-shaped stacked fabric structure distributed in an array to form a green energy environmental control fluid processor module. Since the pyramid structure has a directionality, the monofilaments are almost perpendicular to the air flow direction. Therefore, the electromagnetic wave energy can be effectively used in the scrubber system to reduce the water molecules and increase the surface area of the gas-liquid conversion, and accelerate the gas-liquid conversion time by the torsion field force energy, so as to convert various polluted acid-base gases and liquids, improve the gas-liquid conversion ratio and reduce the height of the HTU mass transfer unit. The technical means adopted to achieve the first object of the present utility model is to include a green energy environmental control fluid processor module provided in the diversion channel system, and the fluid guiding system guides the gas and fluid to be treated into the main diversion channel of the diversion channel system and flows through the green energy environmental control fluid processor module. The green energy environmental control fluid processor module separates the gas-phase fluid and the liquid-phase fluid from the fluid to be treated. The green energy environmental control fluid processor module is selected from at least one of the washing module and the demisting module. The washing module includes at least one washing unit, and the washing unit includes a plurality of washing grids for separating the liquid phase from the gas phase by sticking. The front and back sides of each washing grid are respectively recessed with a first front pyramid-shaped washing groove and a first back pyramid-shaped washing groove distributed in an array. The wall surfaces of each first front pyramid-shaped washing groove and the first back pyramid-shaped washing groove are respectively provided with a first front through-hole washing hole and a first back through-hole washing hole; wherein, the specific surface area of each washing grid for separating the liquid phase from the gas phase is 120~400m 2 / m 3 , the density is 20~60kg / m 3 , the space rate is 90~98%(m 3 ), the total thickness of the stacked plurality of washing grids is 50~4500mm and is transversely arranged in the main diversion channel.

[0006] The second object of the present utility model is to provide a pyramid - type green energy environmental control fluid treatment system, which mainly consists of a catalytic monofilament three - dimensional pyramid - type stacked woven layer structure distributed in an array to form a green energy environmental control fluid processor module. Since the inside of the monofilament contains an environmental control catalyst, under the pyramid - shaped structure, it has the effect of focusing and concentrating energy, which can make small droplets in the air flow collide more easily to form large droplets, removing the fog droplets in the air flow, thus effectively improving the defogging efficiency. Due to the directional structure of the monofilament, which is almost perpendicular to the air flow direction, the fluid to be treated can be effectively separated into a gas - phase fluid to remove the fog droplets in the air flow. The technical means adopted to achieve the second object of the present utility model includes a green energy environmental control fluid processor module provided in a diversion channel system, and the green energy environmental control fluid processor module is selected from at least one of a washing module and a defogging module. The defogging module includes at least one defogging unit. The fluid to be treated is mixed into a liquid - phase fluid by the defogging module, and then the fluid to be treated is separated into a gas - phase fluid and a liquid - phase fluid, and the gas - phase fluid and the liquid - phase fluid are respectively discharged from the exhaust port and the drain port of the diversion channel system. The defogging unit includes a plurality of fluid separation and defogging grids stacked together. The front and back sides of each fluid separation and defogging grid are respectively recessed with first front - side pyramid - shaped defogging grooves and first back - side pyramid - shaped defogging grooves distributed in an array. The walls of each first front - side pyramid - shaped defogging groove and each first back - side pyramid - shaped defogging groove are respectively provided with first front - side through - hole defogging holes and first back - side through - hole defogging holes. The specific surface area of each fluid separation and defogging grid is 400 - 2500 m 2 / m 3 , the density is 20 - 60 kg / m 3 , the porosity is 90 - 98% (m 3 ), and the total thickness of the stack of the plurality of fluid separation and defogging grids for converting the gas phase into the liquid phase is 100 - 600 mm. And it is transversely arranged in the main diversion channel.

[0007] The third object of the present utility model is to provide a pyramid - type high - efficiency green energy environmental control fluid treatment system that effectively reduces pressure loss by using hydrophobic action. The technical means adopted to achieve the third object of the present utility model is to include a green energy environmental control fluid processor module provided in the diversion channel system. The fluid guiding system guides the gas and fluid to be treated into the main diversion channel of the diversion channel system and flows through the green energy environmental control fluid processor module. The green energy environmental control fluid processor module washes the fluid to be treated to separate the liquid - phase fluid, and then separates the gas - phase fluid and the liquid - phase fluid from the fluid to be treated, so that the gas - phase fluid and the liquid - phase fluid are respectively discharged from the exhaust port and the drain port of the diversion channel system. The green energy environmental control fluid processor module is selected from at least one of the washing module and the demisting module. The washing module includes at least one washing unit. The washing unit includes a plurality of washing grids that are stacked together to wash the liquid - phase fluid out of the gas - phase. The front and back sides of each washing grid are respectively recessed with first front - side pyramid - shaped washing grooves and first back - side pyramid - shaped washing grooves that are arranged in an array. The wall surfaces of each first front - side pyramid - shaped washing groove and each first back - side pyramid - shaped washing groove are respectively provided with first front - side through - hole washing holes and first back - side through - hole washing holes; wherein, the specific surface area of each washing grid is 120 - 400m 2 / m 3 , the density is 20 - 60kg / m 3 and the porosity is 90 - 98% (m 3 ). The total thickness of the plurality of stacked washing grids is 50 - 4500mm and is transversely arranged in the main diversion channel. Among them, the specific surface area of each fluid separation and demisting grid of each gas - liquid separation and demisting grid is 400 - 2500m 2 / m 3 , the density is 20 - 60kg / m 3 and the porosity is 90 - 98% (m 3 ). The total thickness of the plurality of stacked gas - phase - converted - to - liquid - phase fluid demisting grids is 100 - 600mm. Among them, the at least one green energy environmental control fluid processor module further includes at least one first demisting grid and at least one second hydrophobic grid; the at least one first hydrophobic grid and the at least one second hydrophobic grid respectively include a plurality of first hydrophobic through - holes and a plurality of second hydrophobic through - holes; the at least one first hydrophobic grid and the at least one second hydrophobic grid respectively coincide with the at least one first fluid separation grid and the at least one second fluid separation grid; the number of the plurality of first hydrophobic through - holes matches and is connected to the number of the plurality of first front - side through - hole separation holes and the plurality of first back - side through - hole separation holes; the number of the plurality of second hydrophobic through - holes matches and is connected to the number of the plurality of second front - side through - hole separation holes and the plurality of second back - side through - hole separation holes.

[0008] The fourth object of the present utility model is to provide a pyramid-shaped high-efficiency green energy environmental control fluid treatment system with an environmental control catalyst antibacterial and mildew-proof woven layer to prevent mildew and inhibit its growth, and to accelerate the decomposition of pollutants by the catalyst to reduce blockage. The technical means adopted to achieve the fourth object of the present utility model is to include a green energy environmental control fluid processor module disposed in a diversion channel system, and a fluid guiding system guides the gas and fluid to be treated into the main diversion channel of the diversion channel system and flows through the green energy environmental control fluid processor module. The green energy environmental control fluid processor module converts the fluid to be treated into a liquid-phase fluid, and then separates the gas-phase fluid and the liquid-phase fluid from the fluid to be treated, so that the gas-phase fluid and the liquid-phase fluid are respectively discharged from the exhaust port and the drain port of the diversion channel system. The green energy environmental control fluid processor module is selected from at least one of a washing module and a demisting module. The washing module includes at least one washing unit, and the washing unit includes a plurality of washing grids that are stacked together to wash and separate the liquid-phase fluid from the gas phase. The front and back sides of each washing grid are respectively recessed with first front pyramid-shaped washing grooves and first back pyramid-shaped washing grooves that are arranged in an array. The wall surfaces of each first front pyramid-shaped washing groove and each first back pyramid-shaped washing groove are respectively provided with first front through-hole washing holes and first back through-hole washing holes; wherein, the specific surface area of each washing grid is 120 - 400 m 2 / m 3 , the density is 20 - 60 kg / m 3 and the space ratio is 90 - 98% (m 3 ), the total thickness of the stacked plurality of washing grids is 50 - 4500 mm and is transversely arranged in the main diversion channel. Among them, the specific surface area of each fluid separation and demisting grid of each gas-liquid separation and demisting grid is 400 - 2500 m 2 / m 3 , the density is 20 - 60 kg / m 3 and the space ratio is 90 - 98% (m 3 ), the total thickness of the stacked plurality of gas-phase to liquid-phase fluid conversion demisting grids is 100 - 600 mm. Among them, there is further included a mildew and bacteria inhibition module; the mildew and bacteria inhibition module is used to act on the washing grids respectively to prevent the washing grids from mildewing and breeding bacteria.

[0009] The fifth object of the present utility model is to provide a pyramid - type high - efficiency green energy environmental control fluid treatment system with the efficacy of enhancing the mixing of pollutants. It mainly utilizes the gas - liquid uniform mixing and gain function with a larger grid to generate a larger turbulent flow effect, enabling water and gas to be more quickly and fully refined and mixed, allowing pollutant particles in the air to be quickly and fully refined and mixed with water droplets, and then entering the demister for separation. The technical means adopted to achieve the fifth object of the present utility model includes a green energy environmental control fluid processor module provided in the diversion channel system. The fluid guiding system guides the gas and fluid to be treated into the main diversion channel of the diversion channel system and flows through the green energy environmental control fluid processor module. The green energy environmental control fluid processor module separates the liquid - phase fluid from the fluid to be treated, and then separates the gas - phase fluid and the liquid - phase fluid from the fluid to be treated, so that the gas - phase fluid and the liquid - phase fluid are respectively discharged from the exhaust port and the drain port of the diversion channel system. The green energy environmental control fluid processor module is selected from at least one of the washing module and the demisting module. The washing module includes at least one washing unit. The washing unit includes a plurality of washing grids that are stacked and adhered to each other for separating the liquid - phase fluid from the gas - phase. The front and back surfaces of each washing grid are respectively recessed with first front - surface pyramid - shaped washing grooves and first back - surface pyramid - shaped washing grooves arranged in an array. The wall surfaces of each first front - surface pyramid - shaped washing groove and first back - surface pyramid - shaped washing groove are respectively provided with first front - surface through - hole washing holes and first back - surface through - hole washing holes. Among them, the specific surface area of each washing grid for separating the liquid - phase fluid from the gas - phase is 120 - 400m 2 / m 3 , the density is 20 - 60kg / m 3 and the space ratio is 90 - 98% (m 3 ). The total thickness of the stacked and adhered plurality of washing grids is 50 - 4500mm and is transversely arranged in the main diversion channel. Among them, it further includes a liquid - phase growth module; the at least one liquid - phase growth module is used to be installed in the diversion channel system and is located between the at least one washing unit and the at least one demisting unit; the liquid - phase growth module includes a plurality of first nozzles and a plurality of second nozzles that are opposite to each other, and the plurality of first nozzles and the plurality of second nozzles are used to spray water mist towards each other.

[0010] Additional aspects and advantages of the present utility model will be given in part in the following description, will become apparent in part from the following description, or will be understood through the practice of the present utility model. BRIEF DESCRIPTION OF THE DRAWINGS

[0011] Figure 1 is a schematic diagram of the implementation of the specific application architecture of the present utility model;

[0012] Figure 2 is a schematic diagram of the basic structure of the washing unit of the present utility model;

[0013] Figure 3It is a schematic diagram of an implementation of the demisting unit of the present utility model;

[0014] Figure 4 It is another schematic diagram of an implementation of the demisting unit of the present utility model;

[0015] Figure 5 It is yet another schematic diagram of an implementation of the demisting unit of the present utility model;

[0016] Figure 6 It is another schematic diagram of an implementation of the washing unit of the present utility model;

[0017] Figure 7 It is a top view schematic diagram of the demisting unit of the present utility model;

[0018] Figure 8 It is a bottom view schematic diagram of the demisting unit of the present utility model;

[0019] Figure 9 It is a functional block schematic diagram of the specific architecture of the present utility model;

[0020] Figure 10 It is a schematic diagram of the result of the differential pressure test experiment for the product model HOP610DS of the present utility model;

[0021] Figure 11 It is a schematic diagram of the overall experimental efficiency for the indoor air quality (IAQ) test of the present utility model;

[0022] Figure 12 It is a schematic diagram of the experimental process for the water removal rate of the present utility model;

[0023] Marking description:

[0024] Diversion channel system 10; exhaust port 11; drain port 12; main diversion channel 13; fluid inlet 130; green energy environmental control fluid processor module 20; washing module 21; washing unit 21a; washing grille 210 for separating liquid phase fluid from gas phase; first front pyramid-shaped washing tank 210a; first back pyramid-shaped washing tank 210b; first front through-hole washing holes 210c; first back through-hole washing holes 210d; demisting module 22; demisting unit 22a; demisting grille 22b for separating liquid phase fluid from gas phase; first fluid separation grille 220; first front pyramid-shaped separation tank 220a; first back pyramid-shaped separation tank 220b; first front through-hole separation holes 220c; first back through-hole separation holes 220d; second fluid separation grille 221; second front pyramid-shaped separation tank 221a; second back pyramid-shaped separation tank 221b; second front through-hole separation holes 221c; second back through-hole separation holes 221d; third fluid separation grille 222; third front pyramid-shaped separation tank 222a; third back pyramid-shaped separation tank 222b; third front through-hole separation holes 222c; third back through-hole separation holes 222d; first hydrophobic grille 23; first hydrophobic through-holes 230; second hydrophobic grille 24; second hydrophobic through-holes 240; anti-mildew and antibacterial module 25; first anti-mildew and antibacterial grille 250; second anti-mildew and antibacterial grille 251; fluid guiding system 30; water spraying and mixing module 40; spray nozzle 41; water spraying and cleaning module 50; sensing module 60; control module 61; liquid phase growth module 70; first nozzle 71; second nozzle 72. Detailed implementation manners

[0025] The embodiments of the present utility model will be described in detail below. The examples of the embodiments are shown in the drawings, wherein the same or similar reference numerals denote the same or similar elements or elements having the same or similar functions throughout. The embodiments described below by referring to the drawings are exemplary and are intended to explain the present utility model, and should not be construed as a limitation to the present utility model.

[0026] In order to better understand the above technical solutions, the exemplary embodiments of the present utility model will be described in more detail below with reference to the drawings. Although the exemplary embodiments of the present utility model are shown in the drawings, it should be understood that the present utility model can be implemented in various forms and should not be limited by the embodiments set forth herein. On the contrary, these embodiments are provided to enable a more thorough understanding of the present utility model and to fully convey the scope of the present utility model to those skilled in the art.

[0027] The following combines the attached Figures 1 - 12 A pyramid-type high-efficiency green energy environmental control fluid processing system provided by the present utility model will be described in detail.

[0028] As Figure 1 AndFigure 2 As shown, for the first embodiment to achieve the first object of the present utility model, it includes a green energy environmental control fluid processor module 20, which is installed on a diversion channel system 10, and a fluid guiding system 30 guides the gas and fluid to be processed into a main diversion channel 13 of the diversion channel system 10 and flows through the green energy environmental control fluid processor module 20. The green energy environmental control fluid processor module 20 processes and separates the liquid-phase fluid from the fluid to be processed, and then separates the gas-phase fluid and the liquid-phase fluid from the fluid to be processed, so that the gas-phase fluid and the liquid-phase fluid are respectively discharged from the exhaust port 11 and the drain port 12 of the diversion channel system 10. The main part of this embodiment is that the green energy environmental control fluid processor module 20 is selected from at least one of the washing module 21 and the demisting module 22. The washing module 21 includes at least one washing unit 21a( Figure 1 In the example, two washing units 21a are disclosed), the at least one washing unit 21a includes a plurality of washing grids 210 that are stacked and adhered to each other to wash and separate the liquid-phase fluid from the gas-phase fluid. A front surface and a back surface of each washing grid 210 for washing and separating the liquid-phase fluid from the gas-phase fluid are respectively recessed to include a plurality of first front pyramid-shaped washing grooves 210a and a plurality of first back pyramid-shaped washing grooves 210b that are arranged in an array. A plurality of first front through-hole washing holes 210c and a plurality of first back through-hole washing holes 210d are respectively provided on the wall surfaces of each of the plurality of first front pyramid-shaped washing grooves 210a and the first back pyramid-shaped washing grooves 210b. Among them, the specific surface area of each washing grid 210 for washing and separating the liquid-phase fluid from the gas-phase fluid is 120 - 400m 2 / m 3 , the density is 20 - 60 kg / m 3 , the porosity is 90 - 98% (m 3 ), and the total thickness (height) of the plurality of stacked and adhered washing grids 210 for washing and separating the liquid-phase fluid from the gas-phase fluid is 50 - 4500 mm and is transverse to the main diversion channel 13. Figure 1 For the two washing units 21a disclosed in the example, starting from the fluid inlet 130 of the main diversion channel 13, they are the first washing unit 21a and the second washing unit 21a. Preferably, the ratio of the total thickness of the first washing unit 21a to the second washing unit 21a is less than 1 / 5 (for example, if the total thickness of the first washing unit 21a is 300 mm, then the total thickness of the second washing unit 21a is greater than 1500 mm), and the ratio of the specific surface area of the first washing unit 21a to the second washing unit 21a is greater than 1.5 (for example, if the specific surface area of the first washing unit 21a is 300 m 2 / m 3 , then the specific surface area of the second washing unit 21a is less than 200 m 2 / m 3), wherein, the first washing unit 21a is used for pre-gas-liquid mixing and filtering impurities, and the second washing unit 21a is used for deep gas-liquid mixing and gas-phase to liquid-phase conversion.

[0029] Combined with Figure 1 、 Figure 3 、 Figure 7 and Figure 8 , this embodiment is the first specific embodiment based on the above-mentioned first embodiment. The demisting module 22 of the green energy environmental control fluid processor module 20 includes at least one demisting unit 22a ( Figure 1 In the example, two demisting units 22a are shown). In a preferred embodiment, the demisting unit 22a includes a plurality of demisting grids 22b for separating liquid phase from gas phase. Among them, the plurality of demisting grids 22b for separating liquid phase from gas phase includes at least one first fluid separation grid 220 (which can be multiple layers; but not limited thereto) and at least one second fluid separation grid 221 (which can be multiple layers; but not limited thereto). The opposite front and back surfaces of the at least one first fluid separation grid 220 are respectively recessed and include a plurality of first front pyramid-shaped separation grooves 220a and a plurality of first back pyramid-shaped separation grooves 220b distributed in an array. The wall surfaces of each of the plurality of first front pyramid-shaped separation grooves 220a are respectively provided with a plurality of first front through-hole separation holes 220c, and the wall surfaces of each of the plurality of first back pyramid-shaped separation grooves 220b are respectively provided with a plurality of first back through-hole separation holes 220d; the opposite front and back surfaces of the at least one second fluid separation grid 221 are respectively recessed and include a plurality of second front pyramid-shaped separation grooves 221a and a plurality of second back pyramid-shaped separation grooves 221b distributed in an array. The wall surfaces of each of the plurality of second front pyramid-shaped separation grooves 221a are respectively provided with a plurality of second front through-hole separation holes 221c, and the wall surfaces of each of the plurality of second back pyramid-shaped separation grooves 221b are respectively provided with a plurality of second back through-hole separation holes 221d; the plurality of first front through-hole separation holes 220c, the plurality of first back through-hole separation holes 220d, the plurality of second front through-hole separation holes 221c, and the plurality of second back through-hole separation holes 221d are communicated; wherein, the specific surface area of the at least one first fluid separation grid 220 is 120 - 400 m 2 / m 3 , the density is 20 - 60 kg / m 3 and the porosity is 90 - 98% (m 3 ), the specific surface area of the at least one second fluid separation grid 221 is 400 - 2250 m 2 / m 3 , the density is 20 - 75 kg / m 3 and the porosity is 90 - 98% (m 3) The at least one first fluid separation grid 220 and the at least one second fluid separation grid 221 are superposed, and the total superposed thickness is 100 to 600 mm and transversely partitions the main flow channel 13, and the washing module 21 is closer to the fluid inlet 130 of the main flow channel 13 than the demisting module 22. In a preferred embodiment, there are a plurality of first fluid separation grids 220 and a plurality of second fluid separation grids 221. The plurality of second fluid separation grids 221 are interposed between the plurality of first fluid separation grids 220. The plurality of first fluid separation grids 220 form an auxiliary support for the plurality of second fluid separation grids 221. The number of the second fluid separation grids 221 is 3 to 10 times the number of the first fluid separation grids 220. Figure 1 In the two demisting units 22a disclosed in the example, starting from the fluid inlet 130 of the main flow channel 13, they are the first demisting unit 22a and the second demisting unit 22a. Preferably, the ratio of the total thickness of the first demisting unit 22a to the total thickness of the second demisting unit 22a is between 0.3 and 0.8 (for example, if the total thickness of the first demisting unit 22a is 150 mm, then the total thickness of the second demisting unit 22a is 187.5 to 500 mm), and the ratio of the specific surface area of the first demisting unit 22a to the specific surface area of the second demisting unit 22a is between 0.25 and 0.5 (for example, if the specific surface area of the first demisting unit 22a is 400 m 2 / m 3 , then the specific surface area of the second demisting unit 22a is between 800 and 1600 m 2 / m 3 ). The density of the first fluid separation grid 220 is 20 to 60 kg / m 3 , and the density of the second fluid separation grid 221 is 20 to 75 kg / m 3 . Among them, the first demisting unit 22a is used for pre-demisting and gas-liquid separation, and the second demisting unit 22a is used for deep demisting and removing white smoke.

[0030] Combined Figure 1 、 Figure 4 、 Figure 7 and Figure 8, this embodiment is a preferred embodiment based on the above first specific embodiment. In addition to having the first fluid separation grid 220 and the second fluid separation grid 221, the demisting unit 22a further includes at least one third fluid separation grid 222 (which can be multiple layers; but not limited thereto). The opposite front and back surfaces of the at least one third fluid separation grid 222 are respectively recessed and include a plurality of third front pyramid-shaped separation grooves 222a and a plurality of third back pyramid-shaped separation grooves 222b arranged in an array. Each wall surface of the plurality of third front pyramid-shaped separation grooves 222a is respectively provided with a plurality of third front through-hole separation holes 222c, and each wall surface of the plurality of third back pyramid-shaped separation grooves 222b is respectively provided with a plurality of third back through-hole separation holes 222d; the plurality of first front through-hole separation holes 220c, the plurality of first back through-hole separation holes 220d, the plurality of second front through-hole separation holes 221c, the plurality of second back through-hole separation holes 221d, the plurality of third front through-hole separation holes 222c and the plurality of third back through-hole separation holes 222d are communicated; wherein, the specific surface area of the at least one first fluid separation grid 220 is 120 - 400m 2 / m 3 , the density is 20 - 60kg / m 3 and the space ratio is 90 - 98% (m 3 ), the specific surface area of the at least one second fluid separation grid 221 is 400 - 1500m 2 / m 3 , the density is 20 - 75kg / m 3 and the space ratio is 90 - 98% (m 3 ), the specific surface area of the at least one third fluid separation grid 222 is 1200 - 2250m 2 / m 3 , the density is 20 - 75kg / m 3 and the space ratio is 90 - 98% (m 3 ); the at least one first fluid separation grid 220, the at least one second fluid separation grid 221 and the at least one third fluid separation grid 222 are stacked in sequence and horizontally partition the main flow channel. In a preferred embodiment, there are a plurality of first fluid separation grids 220, a plurality of second fluid separation grids 221 and a plurality of third fluid separation grids 222. The plurality of second fluid separation grids 221 and the plurality of third fluid separation grids 222 are located between the plurality of first fluid separation grids 220. The plurality of first fluid separation grids 220 form an auxiliary support for the plurality of second fluid separation grids 221 and the plurality of third fluid separation grids 222. The numbers of the second fluid separation grid 221 and the third fluid separation grid 222 are respectively 3 - 6 times the number of the first fluid separation grid 220.

[0031] CombinedFigure 1 , Figure 5 , Figure 7 and Figure 8 , for achieving the second embodiment of the second object of the present utility model, in addition to including the overall technical content of the above-mentioned first embodiment, the green energy environmental control fluid processor module 20 further includes at least one first hydrophobic grid 23 and at least one second hydrophobic grid 24. The at least one first hydrophobic grid 23 and the at least one second hydrophobic grid 24 respectively include a plurality of first hydrophobic through holes (not shown in the figure) and a plurality of second hydrophobic through holes 240. The at least one first hydrophobic grid 23 and the at least one second hydrophobic grid 24 respectively coincide with at least one first fluid separation grid 220 and at least one second fluid separation grid 221. The number of the plurality of first hydrophobic through holes matches and communicates with the number of the plurality of first front-side hollow separation holes 220c and the plurality of first back-side hollow separation holes 220d. The number of the plurality of second hydrophobic through holes 240 matches and communicates with the number of the plurality of second front-side hollow separation holes 221c and the plurality of second back-side hollow separation holes 221d. The at least one first hydrophobic grid 23 and the at least one second hydrophobic grid 24 respectively contain at least 70% by weight of hydrophobic material particles, and the weight percentages of the hydrophobic material particles of the at least one first hydrophobic grid 23 and the at least one second hydrophobic grid 24 respectively correspond to 1-5% of the at least one first fluid separation grid 220 and the at least one second fluid separation grid 221. Among them, the hydrophobic material particles can be 0.1-1% of silicone, silane, SiO 2 , TiO 2 , ZnO-modified PP masterbatch.

[0032] Combined with Figure 1 , Figures 6 - 8, for the third embodiment to achieve the third object of the present utility model, in addition to including the overall technical content of the above first embodiment, this embodiment further includes a mold and bacteria inhibition module 25, and the mold and bacteria inhibition module 25 acts on the plurality of washing grilles 210 for gas-phase washing and separating out liquid-phase fluid, so as to prevent the plurality of washing grilles 210 for gas-phase washing and separating out liquid-phase fluid from mildewing and breeding bacteria. Specifically, the mold and bacteria inhibition module 25 includes a plurality of mold and bacteria inhibition grilles 250 / 251, and the plurality of mold and bacteria inhibition grilles 250 / 251 respectively coincide with the plurality of washing grilles 210 for gas-phase washing and separating out liquid-phase fluid, and keep the plurality of first front-side through-washing holes 210c and the plurality of first back-side through-washing holes 210d unobstructed. More specifically, as an embodiment, each of the plurality of mold and bacteria inhibition grilles 250 / 251 respectively contains at least 70% by weight of mold and bacteria inhibition functional particles, and the weight percentage of the mold and bacteria inhibition functional particles of each mold and bacteria inhibition grille 250 / 251 relative to each of the plurality of washing grilles 210 for gas-phase washing and separating out liquid-phase fluid is 3-35%. The mold and bacteria inhibition functional particles include a catalyst material and at least two of a photoelectric material capable of generating photoelectricity, a piezoelectric material capable of generating piezoelectricity, and a pyroelectric material capable of generating pyroelectricity (such as a far-infrared material). Among them, the photoelectric effect of the photoelectric material is that electromagnetic radiation waves (such as ultraviolet light) irradiate the material, and a photon absorption excitation free electron effect is generated. Mainly, the photoelectric conversion and energy storage phosphor materials with photoelectricity generation and energy storage functions, such as Zn 2 SiO 4 , CaSiO 3 , SiO 2 , TiO 2 , (SrBaMg) 3 Si 2 O 7 , CaWO 4 , MgWO 4 , LiAl 5 O 8 : Mn 4+ , CaAl 2 O 4 : Eu 2+ , Dy 3+ , CaAl 12 O 19 : Mn 4+ , SrAl 2 O 4 : Eu 2+ , Dy 3+ , Sr 4 Al 14 O 25 : Eu 2+ , Dy 3+, SrAl 12 O 19 : Eu 2+ , Dy 3+ , BaMg 2 Al 16 O 27 , CeMgAl 11 O 19 , MgAl 2 O 4 , GdAlO 3 , Y 2 O 3 , YVO 4 , SrB 4 O 7 , F, MgGa 2 O 4 , MgGa 2 O 4 , BeO, MgO, Al 2 O 3 , MgAl 2 O 4 , GeO 2 , SnO 2 , ZnO, Sc 2 O 3 , La 2 O 3 , Sm 2 O 3 , Gd 2 O 3 , Dy 2 O 3 , ZrO 2 , CdS and WO 3 etc. The piezoelectric effect of the piezoelectric materials used is due to the special arrangement of atoms in the crystal lattice, resulting in the coupling effect of the stress field and the electric field. For example, quartz, cadmium sulfide, zinc oxide, aluminum nitride, ferroelectric transistors, barium titanate crystals, lithium niobate, tantalum niobate, strontium barium niobate crystals, potassium dihydrogen phosphate, ammonium dihydrogen phosphate, lead hydrogen phosphate, lead deuterium phosphate crystals, bismuth titanate crystals, barium titanate ceramics, lead zirconate titanate PZT, etc. The thermoelectric materials used are far-infrared materials that can generate far-infrared rays with wavelengths of 4 - 14 μm in the spectrum when receiving external thermal radiation. The wavelength is longer than that of visible light, and it is a thermal induction energy with strong thermal effects. For example, Al 2 O 3 , ZrO 2 , MgO, TiO 2 , SiO 2 , ZrC, SiC, B 4 C, TaC, TiB 2 , ZrB 2 , CrB 2, TiSi 2 , MoSi 2 , WSi 2 , Si 3 N 4 , TiN, Fe 2 O, high-temperature bamboo charcoal, binchotan, hoba stone, Guiyang stone, volcanic rock, jade. The catalyst material used is a catalyst, which can accelerate the chemical reaction rate by providing another reaction pathway with a lower activation energy, and its mass, composition, and chemical properties remain unchanged before and after participating in the chemical reaction. For example, gold, platinum, palladium, rhodium, silver, iron, copper, titanium, nickel, tungsten, zinc, manganese, germanium, bismuth, ruthenium, osmium, iridium, molybdenum, chromium, lanthanum, cerium, praseodymium, neodymium, holmium, carbon nanotubes, etc., and metal oxide catalysts such as titanium oxide, zinc oxide, silicon oxide, titanium oxide, aluminum oxide, iron oxide, palladium oxide, magnesium oxide, zirconium oxide, nickel oxide, tin oxide, manganese oxide, chromium oxide, cerium oxide, neodymium oxide, yttrium oxide, etc.

[0033] Combined Figure 1 with Figure 9 , for the fourth embodiment to achieve the fourth object of the present utility model, in addition to including the overall technical content of the above-mentioned first embodiment, this embodiment further includes at least one liquid-phase growth module 70; the at least one liquid-phase growth module 70 is installed in the diversion channel system 10 and is located between the washing module 21 and the demisting module 22. The liquid-phase growth module 70 includes a plurality of first nozzles 71 and a plurality of second nozzles 72 that face each other, and the plurality of first nozzles 71 and the plurality of second nozzles 72 are used to spray water mist towards each other.

[0034] Combined Figure 1 with Figure 9 , this embodiment is the second specific embodiment based on the above-mentioned first embodiment, and further includes at least one water spraying and mixing module 40. The at least one water spraying and mixing module 40 is used to generate water so that the polluting particles in the fluid to be treated are mixed with the water molecules in the water to form polluted water particles, and are continuously driven by the fluid guiding system 30 to flow through the green energy environmental control fluid processor module 20. The at least one green energy environmental control fluid processor module 20 separates the polluted water particles into a liquid-phase fluid. The at least one water spraying and mixing module 40 can be at least one of a spraying and mixing module and a spraying and mixing module. The spraying and mixing module and the spraying and mixing module respectively include a plurality of spraying nozzles and a plurality of spraying nozzles 41, which are used to spray water or spray on the at least one washing unit 21a; the particle size of the water sprayed by each of the plurality of spraying nozzles is 0.5 - 2 mm, and the particle size of the water sprayed by each of the plurality of spraying nozzles 41 is 0.05 - 0.45 mm.

[0035] Combined Figure 1 with Figure 9, this embodiment is the third specific embodiment based on the above-mentioned second specific embodiment, and further includes at least one water spraying and cleaning module 50, which is used to spray water for cleaning at least one first fluid separation grid 220 and at least one second fluid separation grid 221 in the direction opposite to the flow direction of the fluid to be processed.

[0036] Combined with Figure 1 and Figure 9 , this embodiment is the fourth specific embodiment based on the above-mentioned second specific embodiment, and further includes a sensing module 60 and a control module 61; the sensing module 60 is used to sense the pressure of the fluid to be processed in the main flow channel 13 to generate a pressure sensing signal. The control module 61 is used to receive the pressure sensing signal and convert it into a corresponding pressure value. When the pressure value reaches a preset pressure threshold, the control module 61 generates a control signal to make at least one water spraying and mixing module 40 act more strongly; or start at least one water spraying and cleaning module 50 to act.

[0037] Combined with Figure 1 , this embodiment is the fifth specific embodiment based on the above-mentioned first embodiment. At least one washing unit 21a of the washing module 21 is plural, and at least one demisting unit 22a of the demisting module 22 is also plural.

[0038] More specifically, the gas-liquid conversion of the washing unit 21a should have a wind speed residence of at least 0.5 m / s. For example, the processing air volume is 360,000 CMH, the cylinder diameter is 5000 mm, and the height of the washing layer is 3000 mm. Among them, (A) stage is the washing unit 21a composed of several layers of woven grid gratings stacked together, which is also the catalyst tower packing - gas-liquid mixing stage, and its stacking height is about 1000 - 5000 mm. The main function of the washing unit 21a at this stage is pre-gas-liquid mixing and filtering impurities, with a specific surface area of 120 - 400 m 2 / m 3 , a density of 20 - 60 kg / m 3 and a space rate of 90 - 98%; for example: HOP915 is stacked in 10 layers, with a thickness of 150 mm and a specific surface area of 275 m 2 (m 3 ), and antibacterial and mildew-proof treatment is required. (B) stage is the washing unit 21a composed of several layers of woven grid gratings stacked together, with a stacking height of about 1000 - 10000 mm. The main function of this stage is deep conversion, that is, gas phase to liquid phase, with a specific surface area of 120 - 400 m 2 / m 3 , a density of 20 - 60 kg / m 3 and a space rate of 90 - 98%; for example: HOP930 is stacked in 100 layers with a thickness of 3000 mm and a specific surface area of 136 m 2 (m3 ) Anti-bacterial and anti-mildew treatment is required. Stage (C) consists of the liquid-phase growth module 70, which is also the particle growth stage. Water droplet condensation occurs, and its main functions are liquid-phase growth and auxiliary mutual spraying, turning small droplets into large water droplets again. However, it will increase the probability of white smoke generation and can be used or not used during the process when the effect is not good or in the later stage of the service life (to avoid white smoke generation). 2 / m 3 , with a density of 20 - 60 kg / m 3 and a porosity of 90 - 98%. For example: Usually, there are two layers of 30 mm of HOP915 in the front and back, and 12 layers of 120 mm of HOP410 in the middle, a total of 14 layers with a thickness of 150 mm, and a specific surface area of approximately 350 m 2 (m 3 ), and hydrophobic treatment is required. Stage (E) consists of the demisting module 22 composed of several layers of woven grid gratings stacked together, which is also the hydrophobic demisting layer - gas-liquid separation stage. Its stacking height is about 100 - 400 mm. The main functions of this stage are deep demisting and white smoke removal, with a specific surface area of 350 - 2250 m 2 / m 3 , a density of 20 - 75 kg / m 3 and a porosity of 90 - 98%. For example: Usually, there are 3 layers in the front and back of HOP410, a total of 6 layers with a thickness of 60 mm, 20 layers of 60 mm of HOP203 in the middle, and 20 layers of 40 mm of HOP202 in the middle, a total of 46 layers with a total thickness of 200 mm, and a specific surface area of approximately 1200 m 2 (m 3 ), and hydrophobic treatment is required.

[0039] Combined with Table 1 and Table 2, it is a schematic diagram of the experimental data analysis of the specific surface area, density, porosity, and thickness of several models of woven grid grating products produced by the present utility model.

[0040] Table 1:

[0041]

[0042] Table 2:

[0043]

[0044] To prove the practicality of the green energy environmental control fluid processor module 20 of the present utility model, an experimental example of differential pressure test was conducted on the product model HOP610DS, and the test results are as Figure 10 shown.

[0045] In addition, to verify the practicality of the green energy environmental control fluid processor module 20 of the present utility model, an experimental example of indoor air quality (IAQ) testing was conducted on the product, and the overall efficiency table of the test results is as Figure 11 shown.

[0046] To verify the water removal rate effect of the green energy environmental control fluid processor module 20 of the present utility model, an experimental example of water removal rate testing was conducted on three groups of product models, and the experimental process of the water removal rate is as Figure 12 shown, and the test results are shown in Table 3 below.

[0047] Table 3:

[0048] Number Wind speed (m / s) Differential pressure measurement value (Pa) Measurement value (%) The first group 9.33 951 97.38％ The second group 11.23 992 96.62％ The third group 10.83 990 96.60％

[0049] As can be seen from Table 3, according to the water removal rate test results of the present utility model, using the green energy environmental control filter screen of the present utility model can not only effectively control the pressure difference value, and the water removal rate effect of the filter screen can reach more than 96%; if the natural attenuation rate is deducted, the water removal rate can be as high as more than 99%. Among them, the water removal rate formula is: water removal rate = [(the amount of water collected in the measuring cylinder + the amount of water collected in the black water pipe) / (the amount of water sprayed during the test time - the amount of water that did not pass through the filter screen in the front cabin)] × 100%.

[0050] To verify the water mist removal efficiency of the green energy environmental control fluid processor module 20 of the present utility model, an experimental example of water mist removal efficiency testing was conducted on various product models, and the test results are shown in Table 4 below.

[0051] Table 4:

[0052]

[0053]

[0054] Table 5 is the test report on pressure loss and capture rate of filter products commissioned by the Textile Research Institute; Table 6 is the test report on the relationship between pressure loss and flow rate of filter screen products commissioned by the Textile Research Institute; Table 7 is the test report on filtration efficiency (DEHS) of filter screen products at different particle sizes commissioned by the Textile Research Institute; Table 8 is the test report on filtration efficiency (KCI) of filter screen products at different particle sizes commissioned by the Textile Research Institute.

[0055] Table 5:

[0056]

[0057]

[0058] Table 6:

[0059]

[0060] Table 7:

[0061]

[0062] Table 8:

[0063]

[0064] Table 9 shows the control schematic of the processing air volume and the washing unit 21a (washing layer).

[0065] Table 9:

[0066]

[0067]

[0068] Table 10 is a control schematic of the test of the filter product of the present utility model for the sterilization rate, antiviral and antibacterial efficiency, etc.

[0069] Table 10:

[0070]

[0071] Through the description of the above specific embodiments, the present utility model has the following characteristics:

[0072] 1. The present utility model can be composed of a single-filament three-dimensional pyramid-shaped stacked woven layer structure with an array distribution to form a green energy environmental control fluid processor module. The green energy environmental control fluid processor module is divided into a washing layer and a demisting layer according to different specific surface areas. The main function of the washing layer is to improve gas-liquid conversion, and the main function of the demisting layer is gas-liquid separation. Due to the directional structure, the single filaments are almost perpendicular to the air flow direction, so the fog droplets in the air flow can be effectively removed, and the tower-shaped structure can make the small fog droplets in the air flow easier to collide and form large fog droplets. Therefore, it has the effects of improving the washing and demisting efficiency, improving the phenomenon of viscous blockage caused by the growth of bacteria and molds in semiconductor production, being able to be simply backwashed to increase the service time and reduce maintenance, increasing the catalyst function effect, and the water mist removal efficiency is as high as 98%.

[0073] 2. The present utility model can effectively reduce the pressure loss through hydrophobic action.

[0074] 3. The present utility model has an antibacterial woven layer, and can reduce the blockage of the anti-fog washer through the mildew inhibition effect.

[0075] 4. The present utility model utilizes the basic structure of the functional fiber with the publication number CN101855393A, its manufacturing method, and the fabric made from such fiber, and utilizes the phenomenon that the pyramid energy generates electromagnetic wave cohesive force and generates torsion field force to make the quantum generate disorder phenomenon. This is a currently known physical phenomenon. In addition to the appearance of the pyramid structure, its composition includes piezoelectric materials such as crystals. The green energy environmental control de-fogging scrubber (green eco mat) of the present utility model is made of a pyramid three-dimensional structure 3D fabric added with a catalyst material, which plays the role of enhancing the energy-gathering effect and generating torsion field force to make the quantum generate disorder phenomenon. In an acidic or alkaline gas environment, bacteria and molds are likely to breed, and then grow rapidly to form viscous substances that block the entire scrubbing system or cause backflow and equipment damage. The green energy environmental control scrubbing and de-fogging device of the present utility model utilizes the pyramid structure principle and functional fiber to add a catalyst to generate piezoelectric and pyroelectric phenomena, plays the electromagnetic wave cohesive force phenomenon of the pyramid structure and generates torsion field force to make the quantum generate disorder phenomenon, adopts a three-dimensional conical structure, and promotes a larger specific surface area reaction between the liquid and the gas. Because the fibers are perpendicular to each other, when the liquid drops from the vertical fibers of the three-dimensional cone to the next layer of vertical fibers, new liquid will be formed for surface mass transfer. This network structure forms a grid, making the gas volume and liquid volume more evenly dispersed in a smaller volume after passing through the sieve, and being able to be more converted into uniform flow through different layers, thereby improving the mass transfer efficiency, which is particularly important for the uniform flow process that requires chemical reactions or material separation.

[0076] 5. By using catalyst fibers, the air flow droplets are refined into smaller water molecule clusters, increasing the surface area, improving the gas-liquid conversion, and having a mildew and bacteria inhibition effect to reduce the blockage situation on the washing unit, which is superior to the Raschig ring effect. The product is easy to clean and maintain. In addition to ensuring the long-term stable operation of the product, it also extends the service life of the product.

[0077] 6. On the washing unit, the conversion surface area is increased, the gas-liquid conversion ratio is improved, the mass transfer unit height (HTU) of gas-liquid uniform conversion and flow is reduced, the water molecule clusters are refined to improve the gas-liquid conversion ratio, with excellent mass transfer effect, the HTU efficiency is increased, the washing height is reduced, and the pressure loss is effectively reduced.

[0078] 7. The green energy environmental control de-fogging device removes the fog liquid in the air flow by physical separation method. It is mainly a three-dimensional cone of HDPP (monofilament) single filaments, and the structure has directionality, making almost all of the single filaments perpendicular to the air flow direction. It can effectively remove the fog droplets in the air flow. The conical structure makes the small fog droplets in the air flow easier to collide and form large fog droplets, and the de-fogging efficiency is as high as 97%.

[0079] 8. By combining 3D fabrics composed of three-dimensional conical structures with different pore sizes and wire diameters, which are applicable to various environments and uses, the demister is an important tool for treating tail gas / industrial waste gas. If the demister is blocked, it will lead to excessive pollutant emissions and subsequent extended costs. It has the characteristics of low pressure loss and easy cleaning, and can be cleaned regularly to ensure the filtration efficiency during operation. A demister with high filtration efficiency, medium and low pressure loss (depending on the situation), resistance to strong acids and alkalis, and easy cleaning is provided.

[0080] In the description of the present invention, it should be understood that the orientation or positional relationship indicated by the terms "center", "longitudinal", "transverse", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", etc. is based on the orientation or positional relationship shown in the drawings. It is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus cannot be understood as a limitation of the present invention.

[0081] In addition, the terms "first" and "second" are only used for descriptive purposes and cannot be understood as indicating or implying relative importance or implicitly specifying the quantity of the indicated technical features. Thus, the features defined with "first" and "second" may explicitly or implicitly include one or more of such features. In the description of the present invention, the meaning of "a plurality" is two or more unless otherwise specifically defined.

[0082] In the present invention, unless otherwise clearly specified and limited, the terms "installed", "connected", "connected", "fixed", etc. should be understood in a broad sense. For example, it can be a fixed connection, a detachable connection, or integrated; it can be a mechanical connection or an electrical connection; it can be directly connected or indirectly connected through an intermediate medium, and it can be the communication inside two elements or the interaction relationship between two elements. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.

[0083] In the present invention, unless otherwise clearly specified and limited, the first feature being "above" or "below" the second feature may include the direct contact between the first and second features, or may include the situation where the first and second features are not in direct contact but in contact through other features between them. Moreover, the first feature being "above", "over" and "on" the second feature includes that the first feature is directly above and obliquely above the second feature, or simply means that the horizontal height of the first feature is higher than that of the second feature. The first feature being "below", "beneath" and "under" the second feature includes that the first feature is directly below and obliquely below the second feature, or simply means that the horizontal height of the first feature is lower than that of the second feature.

[0084] In the description of this specification, the descriptions referring to terms such as "one embodiment", "some embodiments", "examples", "specific examples", or "some examples", etc., mean that the specific features, structures, materials, or characteristics described in connection with the embodiment or example are included in at least one embodiment or example of the present utility model. In this specification, the schematic representations of the above terms should not be understood as necessarily referring to the same embodiment or example. Moreover, the specific features, structures, materials, or characteristics described may be combined in any one or more embodiments or examples in a suitable manner. In addition, those skilled in the art can combine and combine the different embodiments or examples described in this specification.

[0085] Although the embodiments of the present utility model have been shown and described above, it can be understood that the above embodiments are exemplary and should not be construed as limiting the present utility model. Those of ordinary skill in the art can make changes, modifications, substitutions, and variations to the above embodiments within the scope of the present utility model.

Claims

1. A pyramid-type green energy environmental control fluid treatment system, comprising a green energy environmental control fluid processor module, which is installed in a guide channel system, and a fluid guide system guides the gas and fluid to be treated into a main guide channel of the guide channel system, and flows through the green energy environmental control fluid processor module, and the green energy environmental control fluid processor module separates the fluid to be treated into gas phase fluid and liquid phase fluid, and then the gas phase fluid and the liquid phase fluid are discharged from an exhaust port and a liquid discharge port of the guide channel system respectively; characterized in that, The green energy environmental control fluid processor module includes at least one of a washing module and a demisting module; the washing module includes at least one washing unit, and the at least one washing unit includes a plurality of overlapping washing grids for washing gas phases to wash out liquid phase fluids, and a plurality of first front pyramid-shaped washing grooves and a plurality of first back pyramid-shaped washing grooves distributed in an array are respectively concavely arranged on a front side and a back side of each of the plurality of washing grids, and a plurality of first front air-permeable washing holes and a plurality of first back air-permeable washing holes are respectively arranged on the wall of each of the plurality of first front pyramid-shaped washing grooves and the first back pyramid-shaped washing groove; wherein the specific surface area of ​​each of the plurality of washing grids is 120 to 400 m 2 / m 3 , density is 20~60kg / m 3 , space rate is 90~98%(m 3 ), the total thickness of the plurality of overlapping washing grilles is 50 to 4500 mm and is separated from the main flow channel; the demisting module includes at least one demisting unit; the at least one demisting unit includes at least one first fluid separation grille and at least one second fluid separation grille; the front and back sides opposite to the at least one first fluid separation grille are respectively provided with a plurality of first front pyramid-shaped separation grooves and a plurality of first back pyramid-shaped separation grooves distributed in an array, and the wall surface of each of the plurality of first front pyramid-shaped separation grooves is respectively provided with a plurality of first front air-permeable separation holes, and the wall surface of each of the plurality of first back pyramid-shaped separation grooves is respectively provided with a plurality of first back air-permeable separation holes The front and back sides opposite to the at least one second fluid separation grid are respectively provided with a plurality of second front pyramid-shaped separation grooves and a plurality of second back pyramid-shaped separation grooves distributed in an array, and the wall surface of each of the plurality of second front pyramid-shaped separation grooves is respectively provided with a plurality of second front air-permeable separation holes, and the wall surface of each of the plurality of second back pyramid-shaped separation grooves is respectively provided with a plurality of second back air-permeable separation holes; the plurality of first front air-permeable separation holes, the plurality of first back air-permeable separation holes, the plurality of second front air-permeable separation holes and the plurality of second back air-permeable separation holes are connected; wherein the specific surface area of ​​the at least one first fluid separation grid is 120-400m 2 / m 3 , density is 20~60kg / m 3 , space rate is 90~98%(m 3 ), the specific surface area of ​​the at least one second fluid separation grid is 400 to 2200 m 2 / m 3 , density is 20~75kg / m 3 , space rate is 90~98%(m 3 ), the at least one first fluid separation grid and the at least one second fluid separation grid are overlapped with a total overlapping thickness of 100 to 600 mm, and are separated from the main flow channel, and the at least one washing unit is closer to a fluid inlet of the main flow channel than the at least one demisting unit.

2. The pyramid-type green energy environmental control fluid treatment system according to claim 1, characterized in that: The washing module includes two washing units, which are a first washing unit and a second washing unit, starting from the fluid inlet of the main flow channel; The ratio of the total thickness of the first washing unit to that of the second washing unit is less than 1 / 5; and the ratio of the specific surface area of ​​the first washing unit to that of the second washing unit is greater than 1.

5.

3. The pyramid-type green energy environmental control fluid treatment system according to claim 1, characterized in that: The demisting module comprises two demisting units, each of which comprises a plurality of first fluid separation grids and a plurality of second fluid separation grids; the plurality of second fluid separation grids are between the plurality of first fluid separation grids; the number of the plurality of second fluid separation grids is 3 to 10 times the number of the plurality of first fluid separation grids; the two demisting units are sequentially a first demisting unit and a second demisting unit starting from the fluid inlet of the main flow channel; the ratio of the total thickness of the first demisting unit to the second demisting unit is between 0.3 and 0.8; the ratio of the specific surface area of ​​the first demisting unit to the second demisting unit is between 0.25 and 0.5; the density of the first fluid separation grid is 20 to 60 kg / m 3 The density of the second fluid separation grid is 20-75 kg / m 3 .

4. The pyramid-type green energy environmental control fluid treatment system according to claim 3, characterized in that: The second demisting unit comprises a plurality of third fluid separation grids; the opposite front and back sides of each third fluid separation grid are respectively provided with a plurality of third front pyramid-shaped separation grooves and a plurality of third back pyramid-shaped separation grooves distributed in an array, the wall surface of each plurality of third front pyramid-shaped separation grooves is respectively provided with a plurality of third front air-permeable separation holes, and the wall surface of each plurality of third back pyramid-shaped separation grooves is respectively provided with a plurality of third back air-permeable separation holes; the plurality of first front air-permeable separation holes, the plurality of first back air-permeable separation holes, the plurality of second front air-permeable separation holes, the plurality of second back air-permeable separation holes, the plurality of third front air-permeable separation holes and the plurality of third back air-permeable separation holes are connected; wherein the specific surface area of ​​the first fluid separation grid is 120-400m 2 / m 3 , density is 20~60kg / m 3 , space rate is 90~98%(m 3 ), the specific surface area of ​​the second fluid separation grid is 400 to 1500 m 2 / m 3 , density is 20~75kg / m 3 , space rate is 90~98%(m 3 ), the specific surface area of ​​the third fluid separation grid is 1200-2200m 2 / m 3 , density is 20~75kg / m 3 , space rate is 90~98%(m 3 ); the plurality of first fluid separation grids, the plurality of second fluid separation grids and the plurality of third fluid separation grids are sequentially overlapped and separated from the main flow channel, the plurality of second fluid separation grids and the plurality of third fluid separation grids are respectively between the plurality of first fluid separation grids, and the number of the plurality of second fluid separation grids and the plurality of third fluid separation grids is respectively 3 to 6 times the number of the plurality of first fluid separation grids.

5. The pyramid-type green energy environmental control fluid treatment system according to claim 1, characterized in that: It also includes a liquid phase growth module; the liquid phase growth module is installed in the guide channel system and is between the washing module and the demisting module; the liquid phase growth module includes a plurality of first nozzles and a plurality of second nozzles relative to each other, and the plurality of first nozzles and the plurality of second nozzles are used to spray water mist towards each other.

6. The pyramid-type green energy environmental control fluid treatment system according to claim 1, characterized in that: The at least one demisting unit further includes at least one first hydrophobic grid and at least one second hydrophobic grid; the at least one first hydrophobic grid and the at least one second hydrophobic grid respectively include a plurality of first hydrophobic through holes and a plurality of second hydrophobic through holes; the at least one first hydrophobic grid and the at least one second hydrophobic grid respectively overlap with the at least one first fluid separation grid and the at least one second fluid separation grid; the plurality of first hydrophobic through holes match the number of the plurality of first front air-permeable separation holes and the plurality of first back air-permeable separation holes and are connected; the plurality of second hydrophobic through holes match the number of the plurality of second front air-permeable separation holes and the plurality of second back air-permeable separation holes and are connected.

7. The pyramid-type green energy environmental control fluid treatment system according to claim 1, characterized in that: The at least one demisting unit also includes at least one third fluid separation grid; a front side and a back side opposite to the at least one third fluid separation grid are respectively provided with a plurality of third front pyramid-shaped separation grooves and a plurality of third back pyramid-shaped separation grooves distributed in an array, and a wall surface of each of the plurality of third front pyramid-shaped separation grooves is respectively provided with a plurality of third front air-permeable separation holes, and a wall surface of each of the plurality of third back pyramid-shaped separation grooves is respectively provided with a plurality of third back air-permeable separation holes; the plurality of first front air-permeable separation holes, the plurality of first back air-permeable separation holes, the plurality of second front air-permeable separation holes, the plurality of second back air-permeable separation holes, the plurality of third front air-permeable separation holes and the plurality of third back air-permeable separation holes are connected; wherein the specific surface area of ​​the at least one first fluid separation grid is 120-400m 2 / m 3 , density is 20~60kg / m 3 , space rate is 90~98%(m 3 ), the specific surface area of ​​the at least one second fluid separation grid is 400 to 1500 m 2 / m 3 , density is 20~75kg / m 3 , space rate is 90~98%(m 3 ), the specific surface area of ​​the at least one third fluid separation grid is 1200-2250m 2 / m 3 , density is 20~75kg / m 3 , space rate is 90~98%(m 3 ); the at least one first fluid separation grid, the at least one second fluid separation grid and the at least one third fluid separation grid are stacked in sequence and have a total thickness of 100 to 600 mm and are separated from the main flow channel.

8. The pyramid-type green energy environmental control fluid treatment system according to claim 1, characterized in that: It also includes an anti-mildew and anti-bacterial module; the anti-mildew and anti-bacterial module includes a plurality of anti-mildew and anti-bacterial grilles; the plurality of anti-mildew and anti-bacterial grilles respectively overlap with the plurality of washing grilles, and keep the plurality of first front-side air-permeable washing holes and the plurality of first back-side air-permeable washing holes transparent.

9. The pyramid-type green energy environmental control fluid treatment system according to claim 1, characterized in that: It also includes at least one water spray mixing module and at least one water spray cleaning module; the at least one water spray mixing module is used to generate water so that the polluted particles in the fluid to be treated are mixed with the water molecules in the water to form polluted water particles, and are continuously driven by the fluid guide system to flow through the green energy environmental control fluid processor module, and the polluted water particles are separated into the liquid phase fluid by the green energy environmental control fluid processor module; the at least one water spray mixing module is at least one of a spray mixing module and a spray mixing module; the spray mixing module and the spray mixing module respectively include a plurality of spray nozzles and a plurality of spray nozzles, which are used to spray water or spray on the at least one washing unit; the at least one water spray cleaning module is used to spray water to clean the at least one first fluid separation grid and the at least one second fluid separation grid in the opposite direction of the flow direction of the fluid to be treated.

10. The pyramid-type green energy environmental control fluid treatment system according to claim 9, characterized in that: It also includes a sensing module and a control module; the sensing module is used to sense the pressure of the fluid to be treated in the main flow channel and generate a pressure sensing signal; the control module is used to receive the pressure sensing signal and convert it into a corresponding pressure value. When the pressure value reaches a preset pressure threshold, the control module generates a control signal to enhance the action of the at least one water spray mixing module; or start the action of the at least one water spray cleaning module.

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